CN205704836U - A kind of production line of powder composition modification machine - Google Patents
A kind of production line of powder composition modification machine Download PDFInfo
- Publication number
- CN205704836U CN205704836U CN201620313133.9U CN201620313133U CN205704836U CN 205704836 U CN205704836 U CN 205704836U CN 201620313133 U CN201620313133 U CN 201620313133U CN 205704836 U CN205704836 U CN 205704836U
- Authority
- CN
- China
- Prior art keywords
- powder composition
- composition modification
- machine
- modification machine
- production line
- 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
Links
Landscapes
- Medicinal Preparation (AREA)
Abstract
The utility model discloses the production line of powder composition modification machine, including powder composition modification machine, also include raw material cabin and heat blower, raw material cabin and heat blower feeding mouth with powder composition modification machine respectively is connected, it is connected between feeding mouth with raw material cabin and has metering feeding device, the discharging opening of powder composition modification machine connects air-introduced machine, it is connected between air-introduced machine with discharging opening and has finished product and dedusting collection device, and the doser being connected with modifier inlet and the dispersant entrance of powder composition modification machine respectively.The production line of powder composition modification agent machine disclosed in this utility model, by arranging air-introduced machine, heat blower make system formed negative pressure, metering feeding device carries out Weighing to powder body, powder composition modification machine carries out dispersing depolymerization to powder body, powder body is fully broken up and complete depolymerization in very short time, and ultimately form unimolecule coating film.Integrate powder drying, grind depolymerization, composite modified and dispersion processes, can accomplish scale production.
Description
Technical field
This utility model relates to powder body material processing equipment field, more particularly, it relates to a kind of powder body is multiple
Close the production line of modifying machine.
Background technology
The use of Inorganic nonmetal mineral powder body material typically just can need to be widely used in after surface modification
The modern macromolecular material such as plastics, rubber, binding agent, high polymer base composite functional material and coating
Deng in industry, the production cost of macromolecular material the most not only can be reduced.Can give product some spy simultaneously
Different physical and chemical performance.But the backward in technique of modifying machine equipment the most seriously constrains China's powder surface modification
The development of technology.
Powder surface modification equipment mainly has the function of three aspects, mixes, disperses, surface modifier
Melt and evenly spread to powder surface, and producing good combination.Kind and character due to mixture
Different, mix, disperse and surface modification require quality index also differ, thus use change
Property equipment is the most different.At present, the modifying surface to powder body, the high cold unit that stirs of general employing realizes,
By add high-power, improve rotating speed, realize strong mixing, be greatly reinforced shearing force, reach strongly to mix
Modified purpose, modifying agent be incorporated as automatic charging after human metering, it is impossible to automatization is enough fully achieved.
The high cold unit that stirs is that intermittent operation produces, and production capacity is less, and product quality is understable.
In sum, how to efficiently solve that powder surface modification equipment capacity is little, product quality not
The problem such as stable, is current those skilled in the art's urgent problem.
Utility model content
In view of this, the purpose of this utility model is to provide the production line of a kind of powder composition modification machine,
Little, the problem of unstable product quality with solution powder surface modification equipment capacity.
In order to achieve the above object, the following technical scheme of this utility model offer:
A kind of production line of powder composition modification machine, including powder composition modification machine, also include respectively with institute
Stating raw material cabin and the heat blower of the feeding mouth connection of powder composition modification machine, described feeding mouth is with described
Connect between raw material cabin and have metering feeding device；
The air-introduced machine being connected with the discharging opening of described powder composition modification machine, described air-introduced machine and described discharging
Connect between Kou and have finished product and dedusting collection device；
The administration dress being connected with modifier inlet and the dispersant entrance of described powder composition modification machine respectively
Put.
Preferably, described metering feeding device includes metering screw conveyer and connects with described raw material cabin respectively
The pressure feeding spiral conveyer connect and LOAD CELLS, one end of described metering screw conveyer and described feed
Conveying worm connects, and the other end of described metering screw conveyer is connected with the inlet tube of described feeding mouth.
Preferably, described doser includes hopper, quantifier, liquefier and compressed air inlet.
Preferably, described finished product and dedusting collection device include sack cleaner, packer, described cloth bag
Cleaner unit is connected through airduct with described discharging opening, and described packer is arranged at the bottom of described sack cleaner.
Preferably, it is characterised in that described powder composition modification machine includes support, air quantity room and motor；
Described air quantity room and described motor are arranged on described support；
Top, described air quantity room is provided with depolymerization wheel, and described depolymerization wheel is internal to be respectively provided with the most successively
There are drying chamber, crushing chamber and modified chamber.
Preferably, described depolymerization wheel top is provided with finished bin, and described discharging opening is positioned in described finished bin.
Preferably, described feeding mouth is positioned on the sidewall of described air quantity room.
Preferably, described modifier inlet and described dispersant entrance lay respectively at the sidewall of described depolymerization wheel
On.
Preferably, the number of described modifier inlet is multiple.
The production line of the powder composition modification machine that this utility model provides, including powder composition modification machine.Also
Including raw material cabin and heat blower, raw material cabin and heat blower respectively with the entering of powder composition modification machine
Material mouth connects, and is connected and has metering feeding device between feeding mouth with raw material cabin, the discharging of powder composition modification machine
Mouthful connecting has air-introduced machine, is connected and has finished product and dedusting collection device between air-introduced machine with discharging opening, and respectively with
The doser that the modifier inlet of powder composition modification machine and dispersant entrance connect.
When the production line of powder composition modification machine of this utility model offer is provided, open air-introduced machine, hot blast
Generator so that system forms negative pressure, and powder body weighed, measures by metering feeding device, after pass through
Feeding mouth is evaporated in entering to powder composition modification machine, pulverizes, and doser passes through modifier inlet
With dispersant entrance powder body it is modified and disperses, the most fully breaing up and complete depolymerization,
And ultimately form unimolecule coating film.The discharging opening of powder composition modification machine connects has finished product to collect with dedusting
Device, carries out dedusting and packaging by this device to finished product, completes the composite modified technique of whole powder body.
It is clear that the production line of the powder composition modification machine of this utility model offer, collect powder drying, grinding
Depolymerization, composite modified and dispersion process in one, serialization degree height, feed automatic gauge, system temperature
Spend the conveying of adjustable, finished gas-flow, can accomplish scale production, and easy and simple to handle, operate steadily, work
Intensity is low.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will
The accompanying drawing used required in embodiment or description of the prior art is briefly described, it should be apparent that,
Accompanying drawing in describing below is only embodiments more of the present utility model, for ordinary skill people
From the point of view of Yuan, on the premise of not paying creative work, it is also possible to obtain the attached of other according to these accompanying drawings
Figure.
The structural representation of the production line of the powder composition modification machine that Fig. 1 provides for this utility model embodiment；
The structural representation of the powder composition modification machine that Fig. 2 provides for this utility model embodiment.
In accompanying drawing, labelling is as follows:
Raw material cabin 1, pressure feeding spiral conveyer 2, metering screw conveyer 3, LOAD CELLS 4, hot blast are sent out
Raw device 5, hopper 6, quantifier 7, liquefier 8, compressed air inlet 9, inlet tube 10, support 11, electricity
Motivation 12, air quantity room 13, modifier inlet 14, dispersant entrance 17, modified chamber 18, discharging opening 19,
Airduct 20, sack cleaner 21, packer 22, air-introduced machine 23, drying chamber 24, feeding mouth 25, pulverizing
Chamber 26.
Detailed description of the invention
This utility model embodiment discloses the production line of a kind of powder composition modification machine, to solve powder body table
Face modified device production capacity is little, the problem of unstable product quality.
Below in conjunction with the accompanying drawing in this utility model embodiment, to the technology in this utility model embodiment
Scheme is clearly and completely described, it is clear that described embodiment is only this utility model one
Divide embodiment rather than whole embodiments.Based on the embodiment in this utility model, this area is common
The every other embodiment that technical staff is obtained under not making creative work premise, broadly falls into this
The scope of utility model protection.
Refer to the production line of the powder composition modification machine that Fig. 1-Fig. 2, Fig. 1 provide for this utility model embodiment
Structural representation；The structural representation of the powder composition modification machine that Fig. 2 provides for this utility model embodiment
Figure.
In a kind of specific embodiment, the production line of powder composition modification machine includes powder composition modification
Machine, also includes raw material cabin 1, heat blower 5, metering feeding device, air-introduced machine 23, finished product and dedusting
Collection device and doser.Wherein, raw material cabin 1 and heat blower 5 respectively with powder composition modification machine
Feeding mouth 25 connect, being connected between feeding mouth 25 with raw material cabin 1 has metering feeding device, and doser is respectively
It is connected with modifier inlet 14 and the dispersant entrance 17 of powder composition modification machine, operationally, first opens
Air-introduced machine 23, makes system form negative pressure, is then turned on heat blower 5, heat blower 5 hot blast temperature
General control is between 110-130 degree, and hot blast sequentially enters the main frame of powder composition modification machine and finished product and removes
In dirt collection device, preheating whole system, after system warm-up, superfine powder is by raw material cabin 1 successively
Enter metering feeding device, after from feeding mouth 25 enter powder composition modification machine carry out breaing up, depolymerization and changing
Property, doser is added in powder composition modification machine by modifier inlet 14 and dispersant entrance 17 and changes
Property agent and dispersant, the powder body after depolymerization is from discharging opening 19 to up to finished product and dedusting collection device, to one-tenth
Product carry out packing processes.
By arranging said apparatus powder body being weighed, packing processes that depolymerization is modified and follow-up, complete
The composite modified production process of whole powder body, the production of the powder composition modification machine that this utility model provides
Line operates under negative pressure, and serialization degree is high, modifying agent is liquefied in advance by doser and is atomized feed,
Feed automatic gauge, system temperature are adjustable, delivery rate is controlled, finished gas-flow carries, no dust pollution,
Can accomplish scale production, and easy and simple to handle, operate steadily, labor intensity low.Simultaneously can be according to modification
The character of agent realizes being automatically adjusted running technology parameter, modification temperature and the time of staying, it is ensured that to micropowder
Body modified effect well and dispersion effect.
General, space velocity size can be changed by the rotating speed of regulation air-introduced machine 23 and the time of staying adjusts
Temperature in joint powder composition modification machine, typically about 100-150 degree, hot blast empties through air-introduced machine 23, heat
The waste heat of wind can be used for preheating and liquefy modifying agent to reach energy-saving and cost-reducing purpose.
Concrete, metering feeding device include metering screw conveyer 3 and be connected with raw material cabin 1 respectively to
Material conveying worm 2 and LOAD CELLS 4, one end of metering screw conveyer 3 and pressure feeding spiral conveyer 2
Connecting, the other end of metering screw conveyer 3 is connected with the inlet tube 10 of feeding mouth 25.In raw material cabin 1
Raw material is weighed by LOAD CELLS 4, when reaching numerical value set in advance, defeated by pressure feeding spiral
Send machine 2 and metering screw conveyer 3 to carry, be delivered to feeding mouth 25 by inlet tube 10, and then arrive powder
Dispersing depolymerization is carried out in bluk recombination modifying machine, general, in other embodiments, it is also possible to by other
Conveyer device carries, and can select voluntarily, all at this utility model according to the actual condition of production
Protection domain in.
Further, doser includes hopper 6, quantifier 7, liquefier 8 and compressed air inlet 9.
The input of modifying agent and dispersant is carried out quantitative setting, with to powder body by arranging hopper 6 and quantifier 7
Modifying agent and the dispersant of middle input accurately calculate, and are carried out modifying agent and dispersant by liquefier 8
Liquefaction, is entered from nozzle spray together with compressed air by compressed air inlet 9, continuous with atomised form
Equably, inject at substantially the same time in the depolymerization wheel of powder composition modification machine, carry out three grades successively and compound change
Property and dispersion process, complete the input process to modifying agent and dispersant.
Further, finished product and dedusting collection device include sack cleaner 21, packer 22, cloth bag
Cleaner unit 21 is connected through airduct 20 with discharging opening 19, and packer 22 is arranged at the bottom of sack cleaner 21.
It is dispersed through the powder body after depolymerization to be exported by the discharging opening 19 of powder composition modification machine, enters in airduct 20,
Sack cleaner 21 is a kind of dry type dust filtration device, it is adaptable to the non-fiber dust that trapping is dried, and utilizes
Dusty gas is filtered by the filtration of fabric, is collected by superfine powder, and by bag
Installation 22 carries out packed products, completes whole technical process.In other embodiments, it is also possible to select it
His device superfine powder can being collected, as long as identical technical purpose can be reached,
Concrete implementation form is not construed as limiting, all in protection domain of the present utility model.
On the basis of the various embodiments described above, powder composition modification machine includes support 11, air quantity room 13 and electricity
Motivation 12；Air quantity room 13 and motor 12 are arranged on support 11；Top, air quantity room 13 is provided with depolymerization wheel,
Depolymerization wheel internal under be respectively arranged with drying chamber 24, crushing chamber 26 and modified chamber 18 successively.Micropowder
Body and hot blast enter drying chamber 24 through feeding mouth 25, general, and the temperature of hot blast controls at 110 degree to 130
Between degree, form turbulent flow at drying chamber 24 rotor high speed rotating, reach quick negative pressure and superfine powder is carried out
Expansion drying, it is possible to realize evaporation and the separation of the residual moisture of 0.5% in powder body so that final in product
Water content reaches the depth drying of 0.05%, processes for follow-up composite modified and dispersion and do after powder body depth drying
Prepare.
Micropowder after depth drying enters crushing chamber 26, and in crushing chamber 26, depolymerization impeller blade is with about 160 metre per second (m/s)s
Linear velocity high-speed rotation, air-introduced machine 23 formed negative pressure under drive powder material high-speed screw shape rise,
Form huge centrifugal force, between sawtooth and atwirl depolymerization impeller blade that depolymerization wheel inwall is static
Few distance about 3mm, therefore, in powder material high-speed screw uphill process, powder body constantly with solution
Huge impact force, frictional force and shearing force is produced between sawtooth and the depolymerization impeller blade of poly-wheel inwall.When
What impact force, frictional force and shearing force were formed make a concerted effort more than the soft-agglomerated surface of sub-micron-powder can time,
Powder granule fully will be broken up and complete depolymerization in very short time.In whole main frame, only depolymerization wheel is
Running device, simple in construction.Operating steadily, it is adaptable to long period safe handling, depolymerization wheel uses carburizing
Process, improve wearability and the service life of equipment.
Concrete, depolymerization wheel top is provided with finished bin, and discharging opening 19 is positioned in finished bin.By being dried,
Finished product powder body after depolymerization carries out discharging by the discharging opening 19 in finished bin, the most also may be used
With according to selecting rationally to arrange the position of discharging opening 19, as long as ensure that finished powder body can normally discharging
, too much restriction is not done in the position that arranges of concrete discharging opening 19.
Further, feeding mouth 25 is positioned on the sidewall of air quantity room 13.The sidewall of air quantity room 13 is arranged
Feeding mouth 25, by heat blower 5 and the combination of air quantity room 13 so that powder body can normally be sucked into powder
In bluk recombination modifying machine, in other embodiments, the position of feeding mouth 25 can also be arranged on powder body be combined
Other positions of modifying machine, as long as ensure that normally sucking of powder body, are generally located on powder body multiple
Closing the bottom of modifying machine, there to be sufficiently large space to carry out composite modified to powder body, its concrete position can
Need to select according to actual production.
Further, modifier inlet 14 and dispersant entrance 17 lay respectively on the sidewall of depolymerization wheel.
General, when mixed and modified, powder body need to be added modifying agent and dispersant to reach modified and scattered
Purpose, completes in being in depolymerization wheel due to the solution poly and modified of powder body, therefore on the sidewall of depolymerization wheel
Modifier inlet 14 and dispersant entrance 17 are set.
Concrete, the number of modifier inlet 14 is multiple.General, the use agent of powder composition modification
Kind more, concrete powder-modified during, multiple modification can be selected according to the actual needs
Agent, and multiple modifier inlet 14 is set to meet Production requirement.
General, the superfine powder after complete depolymerization enters mixed and modified chamber 18 with violent turbulent flow form,
Three kinds of modifying agent and dispersant after liquefaction pass through the compressed air of compressed air inlet 9 respectively from changing simultaneously
Property agent entrance 14 and dispersant entrance 17, with atomised form by continuous-stable, injection the most simultaneously
Modified chamber 18, carries out three grades of composite modified and dispersion process, successively owing to three kinds of modifying agent and dispersant are noted
Fashionable Existential Space position gap is typically about 10-20cm, and the model of powder composition modification agent is different, its position
Put gap also to differ.Therefore, the time that modifying agent contacts with powder body with dispersant there is also small difference
Away from, be conducive to three grades of composite modified and dispersion process successively.Modified chamber 18 is cylindrical structure, without dead angle,
By forming chemical bond or physical entanglement, between surface modifier and dispersant and superfine powder, form one
Firm chemical bond coupling or mechanical-physical are wound around, by consumption and the coefficient of excess of accurate calculation modifying agent,
Form unimolecule coating film.
By using atomization to process modifying agent, when powder material motion is in turbulence state so that material
It is sufficiently mixed with modifying agent, within the 3-5 second, is completed mixed and modified process, shortened in modified chamber 18
The process time, improve clad ratio, improve work efficiency.
General, the process conditions such as the gas flow of powder composition modification machine, main engine power, production capacity
Can need to be adjusted according to actual production, mainly regulate main engine power, air blast by frequency control
Acc power and air-introduced machine 23 power, reach adjust overall apparatus production capacity and reduce the purpose of power consumption.
Its concrete work process is: open air-introduced machine 23, makes system form negative pressure, is then turned on hot blast
Generator 5, hot blast once enters powder composition modification machine host and finished product and dedusting collection device, to whole
System type preheats.After having preheated, superfine powder is sequentially entered quantifier 7, feed spiral shell by raw material cabin 1
Rotation conveyer 2, converges feeding air quantity room 13 drying chamber 24 at inlet tube 10 and compression hot blast.At drying chamber 24
Under rotor high speed rotating, micropowder material forms violent cyclone, material is carried out vacuum flash and is dried, real
The evaporation of existing residual moisture and separation.
Micropowder after depth drying enters crushing chamber 26, micropowder in high-speed screw uphill process, constantly with
Producing impact force, frictional force and shearing force between depolymerization wheel inwall stator and depolymerization impeller blade, powder granule will
Fully broken up and complete depolymerization at short notice.
The completely superfine powder after depolymerization enters modified chamber 18 with turbulent flow form, the modifying agent after liquefaction and point
Powder is entered from four nozzle spray respectively by compressed air inlet 9, with atomised form by continuous uniform,
Inject mixed and modified chamber 18 at substantially the same time, carry out three grades of composite modified and dispersion process, powder body things successively
Material motion morphology is in turbulence state again, so that material is sufficiently mixed with modifying agent, mixing changes
The time of property process is about the 3-5 second, and amount of modifier is about 0.8%-1.2%, and forms unimolecule coating film.
The production line of powder composition modification machine that this utility model provides is primarily adapted for use in stearic acid, various
Coupling agents etc. are to calcium carbonate, potter's clay, bentonite, iron oxide red, Talcum, Muscovitum, Kaolin, quartz, silicon
The nonmetal mineral fillers such as lime stone, titanium dioxide carries out the most composite modified and dispersion process, its modified effect
Preferable with processing performance.
The production line of whole powder composition modification agent operates under negative pressure, and serialization degree is high, modifying agent is pre-
First liquefy and be atomized feed, feed automatic gauge, system temperature is adjustable, delivery rate is controlled, finished product gas
Stream conveying, no dust pollution, can accomplish scale production, and easy and simple to handle, operate steadily, work strong
Spend low, meanwhile, can realize being automatically adjusted running technology parameter according to the character of modifying agent, modification temperature and
The time of staying, it is ensured that to superfine powder modified effect well and dispersion effect.
In this specification, each embodiment uses the mode gone forward one by one to describe, and each embodiment stresses
Being the difference with other embodiments, between each embodiment, identical similar portion sees mutually.
Described above to the disclosed embodiments, makes professional and technical personnel in the field be capable of or uses
This utility model.Multiple amendment to these embodiments will be aobvious for those skilled in the art
And be clear to, generic principles defined herein can be without departing from spirit or scope of the present utility model
In the case of, realize in other embodiments.Therefore, this utility model is not intended to be limited to institute herein
These embodiments shown, and it is to fit to consistent with principles disclosed herein and features of novelty the widest
Scope.
Claims (9)
1. the production line of a powder composition modification machine, including powder composition modification machine, it is characterized in that: also include raw material cabin (1) and the heat blower (5) being connected with the feeding mouth (25) of described powder composition modification machine respectively, be connected between described feeding mouth (25) with described raw material cabin (1) and have metering feeding device；
The air-introduced machine (23) being connected with the discharging opening (19) of described powder composition modification machine, is connected between described air-introduced machine (23) with described discharging opening (19) and has finished product and dedusting collection device；
The doser being connected with modifier inlet (14) and the dispersant entrance (17) of described powder composition modification machine respectively.
The production line of powder composition modification machine the most according to claim 1, it is characterized in that, described metering feeding device includes metering screw conveyer (3) and the pressure feeding spiral conveyer (2) being connected respectively and LOAD CELLS (4) with described raw material cabin (1), one end of described metering screw conveyer (3) is connected with described pressure feeding spiral conveyer (2), and the other end of described metering screw conveyer (3) is connected with the inlet tube (10) of described feeding mouth (25).
The production line of powder composition modification machine the most according to claim 2, it is characterised in that described doser includes hopper (6), quantifier (7), liquefier (8) and compressed air inlet (9).
The production line of powder composition modification machine the most according to claim 3, it is characterized in that, described finished product and dedusting collection device include sack cleaner (21), packer (22), described sack cleaner (21) is connected through airduct (20) with described discharging opening (19), and described packer (22) is arranged at the bottom of described sack cleaner (21).
5. according to the production line of the powder composition modification machine described in any one of claim 1-4, it is characterised in that described powder composition modification machine includes support (11), air quantity room (13) and motor (12)；
Described air quantity room (13) and described motor (12) are arranged on described support (11)；
Described air quantity room (13) top is provided with depolymerization wheel, and described depolymerization wheel is internal is respectively arranged with drying chamber (24), crushing chamber (26) and modified chamber (18) the most successively.
The production line of powder composition modification machine the most according to claim 5, it is characterised in that described depolymerization wheel top is provided with finished bin, and described discharging opening (19) is positioned in described finished bin.
The production line of powder composition modification machine the most according to claim 6, it is characterised in that described feeding mouth (25) is positioned on the sidewall of described air quantity room (13).
The production line of powder composition modification machine the most according to claim 7, it is characterised in that described modifier inlet (14) and described dispersant entrance (17) lay respectively on the sidewall of described depolymerization wheel.
The production line of powder composition modification machine the most according to claim 8, it is characterised in that the number of described modifier inlet (14) is multiple.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620313133.9U CN205704836U (en) | 2016-04-14 | 2016-04-14 | A kind of production line of powder composition modification machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620313133.9U CN205704836U (en) | 2016-04-14 | 2016-04-14 | A kind of production line of powder composition modification machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205704836U true CN205704836U (en) | 2016-11-23 |
Family
ID=57308061
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620313133.9U Expired - Fee Related CN205704836U (en) | 2016-04-14 | 2016-04-14 | A kind of production line of powder composition modification machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205704836U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105773873A (en) * | 2016-04-14 | 2016-07-20 | 长沙万荣粉体设备科技有限公司 | Production line of powder compound modification machine |
| CN107377156A (en) * | 2017-06-12 | 2017-11-24 | 湖州科祥新材料有限公司 | Air-flow depolymerization modifying machine and its method of work |
| CN107805410A (en) * | 2017-11-24 | 2018-03-16 | 锦州钛业股份有限公司 | A kind of titanium white production method improved in resin system dispersiveness |
| CN109133186A (en) * | 2018-11-09 | 2019-01-04 | 长沙万荣粉体设备科技有限公司 | A kind of iron oxide red production and processing system |
| CN109370259A (en) * | 2018-11-09 | 2019-02-22 | 长沙万荣粉体设备科技有限公司 | A kind of modified calcium carbonate dry powder production system and method |
| CN115321550A (en) * | 2022-10-12 | 2022-11-11 | 广州维桢化工科技有限公司 | Kaolin drying/cooling and modifying integrated device and kaolin processing method |
-
2016
- 2016-04-14 CN CN201620313133.9U patent/CN205704836U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105773873A (en) * | 2016-04-14 | 2016-07-20 | 长沙万荣粉体设备科技有限公司 | Production line of powder compound modification machine |
| CN107377156A (en) * | 2017-06-12 | 2017-11-24 | 湖州科祥新材料有限公司 | Air-flow depolymerization modifying machine and its method of work |
| CN107805410A (en) * | 2017-11-24 | 2018-03-16 | 锦州钛业股份有限公司 | A kind of titanium white production method improved in resin system dispersiveness |
| CN107805410B (en) * | 2017-11-24 | 2020-07-07 | 中信钛业股份有限公司 | Titanium dioxide production method for improving dispersibility in resin system |
| CN109133186A (en) * | 2018-11-09 | 2019-01-04 | 长沙万荣粉体设备科技有限公司 | A kind of iron oxide red production and processing system |
| CN109370259A (en) * | 2018-11-09 | 2019-02-22 | 长沙万荣粉体设备科技有限公司 | A kind of modified calcium carbonate dry powder production system and method |
| CN115321550A (en) * | 2022-10-12 | 2022-11-11 | 广州维桢化工科技有限公司 | Kaolin drying/cooling and modifying integrated device and kaolin processing method |
| CN115321550B (en) * | 2022-10-12 | 2022-12-13 | 广州维桢化工科技有限公司 | Kaolin drying/cooling and modifying integrated device and kaolin processing method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205704836U (en) | A kind of production line of powder composition modification machine | |
| CN105773873A (en) | Production line of powder compound modification machine | |
| CN102358705B (en) | Process for producing sintered ceramsite by using solid waste materials, and system thereof | |
| CN100579879C (en) | Delivery spray nozzle, polytetrafluoroethylene fine particle processing method and apparatus using the spray nozzle | |
| CN206207919U (en) | Color sand production system | |
| CN104001450A (en) | Rotating bucket type granulator | |
| CN207562985U (en) | A kind of new flour miller | |
| CN109129878A (en) | A kind of preparation facilities of ceramic material | |
| CN208944044U (en) | A kind of flyash wet granulation device | |
| CN209699481U (en) | A kind of preparation facilities of PC pavement brick | |
| CN100345618C (en) | Continuous powdery humidifying contrifugal granulator and process thereof | |
| CN208899276U (en) | A kind of Multifunctional continuous bituminous mixture equipment | |
| CN203899566U (en) | Rotary drum type granulator | |
| CN206955910U (en) | A kind of process units of the superfine composite material of concrete | |
| CN109227924A (en) | A kind of ceramic material synthesis device | |
| CN105732001A (en) | Fly ash ceramsite pelletizing-process production method using stainless steel belt type roasting machine | |
| CN109160817A (en) | A kind of manufacturing equipment of ceramic material | |
| CN210813962U (en) | Seasoning production system | |
| CN108162234A (en) | The method for solving the fervent high-viscosity material particle agglomeration phenomenon of die face | |
| CN207872101U (en) | A kind of novel comminutor | |
| CN209459425U (en) | A kind of metallurgy forming agent rotation material-strewing device | |
| CN107377156A (en) | Air-flow depolymerization modifying machine and its method of work | |
| CN209141188U (en) | A kind of plastic film special color master batch preparation facilities with Kekelé structure count | |
| CN103920643A (en) | Method for product grading in polychlorostyrene paste resin production | |
| CN206718258U (en) | A kind of integrated apparatus of crushing and screening insulator silicon rubber |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161123 Termination date: 20190414 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |