CN205850788U - Gas-liquid biphase system is for the equipment of powder body - Google Patents
Gas-liquid biphase system is for the equipment of powder body Download PDFInfo
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- CN205850788U CN205850788U CN201620736248.9U CN201620736248U CN205850788U CN 205850788 U CN205850788 U CN 205850788U CN 201620736248 U CN201620736248 U CN 201620736248U CN 205850788 U CN205850788 U CN 205850788U
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Abstract
The utility model proposes a kind of gas-liquid biphase system equipment for powder body, including raw material annealing device, mixing arrangement and spray equipment；Described mixing arrangement includes mixing chamber, the first Laval nozzle and the second Laval nozzle；The top of described mixing chamber is run through and is arranged described first Laval nozzle, and the bottom of described mixing chamber connects described second Laval nozzle；Described second Laval nozzle end is passed through described spray equipment；Described raw material annealing device is by the raw material mixing of different physical states, and is connected the mixing chamber of described mixing arrangement by conduit.The gas-liquid biphase system provided in this utility model, for the equipment of powder body, can make raw material be sufficiently mixed so that the powder body material activity of preparation is high, and powder granularity is little, and can prepare composite powder material.
Description
Technical field
This utility model relates to powder body material and manufactures field, particularly to a kind of gas-liquid biphase system for the equipment of powder body.
Background technology
Powder body material is important product form, and national economy and national defence are produced important function.Particle technology is the widest
General it is applied to building materials, machinery, the energy, plastics, rubber, mine, metallurgy, medicine, food, feedstuff, pesticide, chemical fertilizer, papermaking, money
The every field of the almost national economic development such as source, environmental protection, information, Aeronautics and Astronautics, traffic.
At present, power production mode has two kinds: one, and solid phase produces powder body, such as grinding；But the powder body of grinding,
Particle size distribution is wide in range, and does not possess chemism.Two, liquid-phase precipitation method prepares powder body, and this powder body has chemism；But deposit
High at impurity content, pollute water and soil, it is impossible to manufacture the problem such as metal-powder, metal composite powder body.
Utility model content
Main purpose of the present utility model, for providing a kind of gas-liquid biphase system for the equipment of powder body, can make raw material the most mixed
Close so that the powder body material activity of preparation is high, and powder granularity is little, and can prepare composite powder material.
The utility model proposes a kind of gas-liquid biphase system equipment for powder body, including raw material annealing device, mixing dress
Put and spray equipment；
Described mixing arrangement includes mixing chamber, the first Laval nozzle and the second Laval nozzle；Described mixing chamber
Top is run through and is arranged described first Laval nozzle, and the bottom of described mixing chamber connects described second Laval nozzle；Described
Two Laval nozzle ends are passed through described spray equipment；
Described raw material annealing device is by the raw material mixing of different physical states, and connects described mixing by conduit
The mixing chamber of device.
Further, described raw material annealing device includes that preheating cabinet, master add hot tank and thermal balance case；Described preheating
Raw material is heated to liquid by case, and described master adds hot tank and raw material is heated to gaseous state；
Bottom described preheating cabinet and main heating bottom portion connects described thermal balance case, described thermal balance by conduit respectively
Bottom portion connects described mixing chamber by conduit.
Further, described preheating cabinet includes the first casing, the first heating jacket and the first electromagnetic wave transmitter；Described
Main heating case includes the second casing, the second heating jacket and the second electromagnetic wave transmitter；Described thermal balance case includes the 3rd case
Body, the 3rd heating jacket and the 3rd electromagnetic wave transmitter；
Described first casing periphery arranges described first heating jacket, and described first box bottom connects described by conduit
3rd casing, the bottom of described first casing differs from catheter position and arranges described first electromagnetic wave transmitter；Described second casing
Periphery arranges described second heating jacket, and described second box bottom connects described 3rd casing, described second case by conduit
The bottom of body differs from catheter position and arranges described second electromagnetic wave transmitter；The periphery of described 3rd casing arranges described Acanthopanan trifoliatus (L.) Merr.
Thermal jacket, the bottom sides of described 3rd casing connects described mixing chamber by conduit, and described 3rd box bottom arranges described
3rd electromagnetic wave transmitter.
Further, described mixing arrangement also includes that the 4th heating jacket, described 4th heating jacket are coated on described mixing
Close room, the first Laval nozzle and the second Laval nozzle peripheral, and the top of described 4th heating jacket is corresponding with bottom
It is provided with fixing described first Laval nozzle and the opening of the second Laval nozzle.
Further, described spray equipment includes spray booth, arranges conveyer belt, main spray booth and powder in described spray booth
Body thickness actuator；
Described main spray booth is arranged in the middle part of described spray booth, and described main jet is coated with ceiling portion and is provided with for described second Bearing score
The opening that your nozzle tip is passed through, described main jet is coated with the lower section of indoor second Laval nozzle end and arranges described conveyer belt；Institute
The one end stating conveyer belt is provided above described powder thickness actuator, and described powder thickness actuator is fixed on described main spray booth
Side bottom, and and described conveyer belt between set the thickness of material layer on clearance control conveyer belt.
Further, described spray equipment also includes heat exchanger；
Described heat exchanger is arranged in described conveyer belt internal voids and carries out heat friendship with the material on its upper conveyor
Change.
Further, described spray equipment also includes material collecting device；Described material collecting device includes conveyor belt cleaner, powder body
Collecting chamber and vibrating screen panel；
Described conveyer belt transmits end and connects described powder body collecting chamber, and is provided with the cleaning transmission of described conveyor belt cleaner
Band；Described powder body collecting chamber lower end is provided with opening and houses described vibrating screen panel；Described vibrating screen panel includes screen cloth and vibrations
Motor, described vibrations motor drives the vibrations of described screen cloth.
Further, described equipment also includes that matrix material discharging device, described matrix material discharging device include pre-place
Reason room and heating chamber；Described pretreatment chamber connects described heating chamber, arranges a conduit and be passed through described spray bottom described heating chamber
It is coated with indoor, and is positioned at above the initiating terminal of described conveyer belt；
Bottom described heating chamber, the end of conduit arranges a nozzle.
Further, described equipment also includes that protective atmosphere processing means, described protective atmosphere processing means include protection
Gas heating chamber and atmosphere source chamber；
Described atmosphere source chamber connects described protective gas heating chamber, and described protective gas heating chamber lower end arranges a conduit and leads to
Enter described main jet and be coated with indoor.
Further, described equipment also includes that carrier gas processing system, described carrier gas processing system include carrier gas room, oil removing
Device, dehydrater and carrier gas heating chamber, described carrier gas room, dehydrater, grease trap and carrier gas heating chamber be sequentially connected with, described load
Gas heating chamber lower end arranges opening and connects the top of described first Laval nozzle.
The gas-liquid biphase system provided in this utility model, for the equipment of powder body, has the advantages that
The gas-liquid biphase system provided in this utility model, for the equipment of powder body, uses electromagnetic wave transmitter auxiliary heating, lives
Change, mixed raw material, on the basis of energy-saving and cost-reducing, the material of metal or other indissolubles is heated to liquid, gaseous state, etc. from
Sub-state, Supercritical Conditions.Therefore, it can manufacture the multiple materials such as composition metal powder body material, Graphene；Application Bearing score
The principle of your jet pipe high velocity, low pressure, raw material and high pressure carrier gas mix at mixing chamber, are conducive to the most quickly mixing, joint
The about equipment such as pump；The use of Laval nozzle, can accelerate to velocity of sound by the highest for high pressure carrier gas, and beneficially high degree of dispersion is different
The material of state, reaches the other mixed-scale of molecular level, sprays to conveyer belt and can obtain ultra-fine grain, and table specific area is big, alive
Property high.Carrier gas, raw material, matrix material all can carry out pretreatment, it is ensured that the high-purity of powder body.
Accompanying drawing explanation
Fig. 1 be in this utility model embodiment gas-liquid biphase system for the device structure schematic diagram of powder body；
Fig. 2 is Laval nozzle structural representation in this utility model embodiment.
The realization of this utility model purpose, functional characteristics and advantage will in conjunction with the embodiments, are described further referring to the drawings.
Detailed description of the invention
Should be appreciated that specific embodiment described herein, only in order to explain this utility model, is not used to limit this
Utility model.
With reference to Fig. 1, for gas-liquid biphase system in this utility model embodiment for the device structure schematic diagram of powder body.
This utility model embodiment proposes a kind of gas-liquid biphase system equipment for powder body, including raw material annealing device
1, mixing arrangement 2 and spray equipment 3；
Above-mentioned mixing arrangement 2 includes mixing chamber the 20, first Laval nozzle 21 and the second Laval nozzle 22；Above-mentioned mixed
The top closing room 20 is run through and is arranged above-mentioned first Laval nozzle 21, and the bottom of above-mentioned mixing chamber 20 connects above-mentioned second Lavalle
Jet pipe 22；Above-mentioned second Laval nozzle 22 end is passed through above-mentioned spray equipment 3.
In the present embodiment, Laval nozzle includes the first Laval nozzle 21 and the second Laval nozzle 22, first
Laval nozzle 21 and the second Laval nozzle 22 structure are identical, all include collapsible tube 200, trunnion 201 and expansion pipe 202
(with reference to Fig. 2), above-mentioned collapsible tube 200 is the most diminishing structure, and above-mentioned trunnion 201 is collapsible tube 200 and expansion
The junction of pipe 202, above-mentioned expansion pipe 202 is the structure the most gradually expanded.Gases at high pressure enter warp from collapsible tube 200
Expansion pipe 202 sprays, and can form the atmosphere of high velocity, low pressure.Be conducive to the material of high degree of dispersion different conditions, reach molecule
The mixed-scale of rank, sprays to conveyer belt and can obtain ultra-fine grain, and its table specific area is big, activity is high.
Above-mentioned raw material annealing device 1 is by the raw material mixing of different physical states, and connects above-mentioned by conduit 10
The mixing chamber 20 of mixing arrangement 2.
In the present embodiment, raw material is mixed by raw material annealing device 1, the first Laval nozzle of mixing arrangement 2
The collapsible tube 200 of 21 is passed through gases at high pressure, and stretched pipe 202 sprays, and forms high velocity, low pressure atmosphere, by former material in mixing chamber 20
Raw material in material annealing device 1 sucks, and beneficially raw material the most quickly mixes with gas, has saved the equipment such as pump.
Further, above-mentioned raw material annealing device 1 includes that preheating cabinet, master add hot tank and thermal balance case；Above-mentioned pre-
Raw material is heated to liquid by hot tank, and above-mentioned master adds hot tank and raw material is heated to gaseous state, plasma state, supercritical fluid shape
State.
Bottom above-mentioned preheating cabinet and main heating bottom portion connects above-mentioned thermal balance case by conduit 10 respectively, and above-mentioned heat is put down
Weighing apparatus bottom portion connects above-mentioned mixing chamber 20 by conduit 10.
Further, above-mentioned preheating cabinet includes the first casing the 11, first heating jacket 12 and the first electromagnetic wave transmitter
13；Above-mentioned main heating case includes the second casing the 14, second heating jacket 15 and the second electromagnetic wave transmitter 16；Above-mentioned thermal balance
Case includes the 3rd casing the 17, the 3rd heating jacket 18 and the 3rd electromagnetic wave transmitter 19；Above-mentioned first heating jacket 12 is will
Raw material is heated to the high temperature heater (HTH) of liquid, and above-mentioned second heating jacket 15 is that the superhigh temperature that raw material is heated to gaseous state adds
Hot device.Above-mentioned first electromagnetic wave transmitter the 13, second electromagnetic wave transmitter 16 and the 3rd electromagnetic wave transmitter 19 are for sending out
Penetrate microwave, medium wave, long wave, shortwave, laser, infrared ray, ultraviolet, visible ray, alpha ray, β ray, gamma ray, sound wave, surpass
Sound wave, the electromagnetic wave transmitter 19 of infrasonic wave one or more of which.Electromagnetic wave transmitter 19 auxiliary is used to heat, activate, mix
Close raw material, on the basis of energy-saving and cost-reducing, the material of metal or other indissolubles is heated to liquid, gaseous state, plasma shape
State, Supercritical Conditions.Therefore, it can manufacture the multiple materials such as composition metal powder body material, Graphene.
Above-mentioned first casing 11 periphery arranges above-mentioned first heating jacket 12, by conduit 10 bottom above-mentioned first casing 11
Connecting above-mentioned 3rd casing 17, the bottom of above-mentioned first casing 11 differs from conduit 10 position and arranges above-mentioned first electromagnetic wave transmitter
13；Above-mentioned second casing 14 periphery arranges above-mentioned second heating jacket 15, is connected by conduit 10 bottom above-mentioned second casing 14
Above-mentioned 3rd casing 17, the bottom of above-mentioned second casing 14 differs from conduit 10 position and arranges above-mentioned second electromagnetic wave transmitter 16；
The periphery of above-mentioned 3rd casing 17 arranges above-mentioned 3rd heating jacket 17, and the bottom sides of above-mentioned 3rd casing 17 passes through conduit 10
Connect above-mentioned mixing chamber 20, bottom above-mentioned 3rd casing 17, above-mentioned 3rd electromagnetic wave transmitter 19 is set.Above-mentioned first casing 11
Connect with the second casing 14, in the first casing 11 and the second casing 14, house the raw material of liquid, gaseous state respectively；3rd casing 14
Raw material within mixing the first casing 11 and the second casing 14.Above-mentioned conduit 10 can also arrange the dresses such as the switch valve of necessity
Put.
Further, above-mentioned mixing arrangement 2 also includes that the 4th heating jacket 23, above-mentioned 4th heating jacket 23 are coated on
State outside mixing chamber the 20, first Laval nozzle 21 and the second Laval nozzle 22, and the top of above-mentioned 4th heating jacket 23
Portion and bottom are correspondingly arranged on fixing above-mentioned first Laval nozzle 21 and the opening of the second Laval nozzle 22.In this enforcement
In example, the collapsible tube 200 of above-mentioned first Laval nozzle 21 of open top fixed clamp of above-mentioned 4th heating jacket 23, above-mentioned
The expansion pipe 202 of the first Laval nozzle 21 is placed in mixing chamber 20.The bottom opening of above-mentioned 4th heating jacket 23 is fixed
Clamping the collapsible tube 200 of above-mentioned second Laval nozzle 21, the expansion pipe 202 of above-mentioned second Laval nozzle 21 highlights above-mentioned
Outside the bottom of four heating jackets 23.
Further, above-mentioned spray equipment 3 includes spray booth, arranges conveyer belt 33, main spray booth 30 in above-mentioned spray booth
And powder thickness actuator 34；
Above-mentioned main spray booth 30 is arranged in the middle part of above-mentioned spray booth, and the both sides of main spray booth 30 arrange blowing room 31 and receive
Material room 32.Above-mentioned main spray booth 30 top is provided with the opening being passed through for above-mentioned second Laval nozzle 22 end, above-mentioned main jet
In painting room 30, the lower section of the second Laval nozzle 22 end arranges above-mentioned conveyer belt 33, and this conveyer belt 33 is across being arranged at above-mentioned master
Spray booth 30, blowing room 31 and bottom, rewinding room 32；One end of above-mentioned conveyer belt 33 is provided above the regulation of above-mentioned powder thickness
Device 34, above-mentioned powder thickness actuator 34 is fixed on above-mentioned main spray booth 30 side bottom, and and above-mentioned conveyer belt 33 between set
Fixed gap controls the thickness of material layer on conveyer belt 33.Above-mentioned powder thickness actuator 34 is fixed on main spray booth sidewall, with
Set certain height distance between conveyer belt, only allow the dusty material setting thickness to pass through.This powder thickness actuator 34
Can be a brush, it is also possible to be a scraper plate, or the device of other identical functions.
Further, above-mentioned spray equipment 3 also includes heat exchanger 35；
Above-mentioned heat exchanger 35 is arranged in above-mentioned conveyer belt 33 internal transmission space and the material on its upper conveyor 33
Material carries out heat exchange.In the present embodiment, above-mentioned heat exchanger 35 is arranged at the back side of the upper strata conveyer belt of above-mentioned conveyer belt 33.Base
Body material to transmitting end, carries out heat exchange with heat exchanger 35 from the transmission of conveyer belt 33 initiating terminal.Above-mentioned heat exchanger 35 was both
Material on conveyer belt 33 can be heated, it is also possible to absorb its heat.
Further, above-mentioned spray equipment 3 also includes material collecting device；Material collecting device is arranged in above-mentioned rewinding room, above-mentioned
Material collecting device includes conveyor belt cleaner 36, powder body collecting chamber 37 and vibrating screen panel 38；
Above-mentioned conveyer belt 33 transmits end and connects above-mentioned powder body collecting chamber 37, and it is clear to be provided with above-mentioned conveyor belt cleaner 36
Clean conveyer belt；This conveyor belt cleaner 36 can be the devices such as powder brush.Above-mentioned powder body collecting chamber 37 lower end is provided with opening
Accommodating above-mentioned vibrating screen panel 38；Above-mentioned vibrating screen panel 38 includes screen cloth and vibrations motor, and above-mentioned vibrations motor drives above-mentioned sieve
Net vibrations.
Further, the said equipment also includes matrix material discharging device 4, and above-mentioned matrix material discharging device 4 includes pre-
Process chamber 41 and heating chamber 42；Above-mentioned pretreatment chamber 41 connects above-mentioned heating chamber 42, arranges one and lead bottom above-mentioned heating chamber 42
Pipe 10 is passed through in above-mentioned spray booth, and is positioned at above the initiating terminal of above-mentioned conveyer belt 33；To matrix material in above-mentioned pretreatment chamber 41
Material sieves, and prevents bulky grain from entering spray booth；Matrix material is heated to assigned temperature by heating chamber 42.Pretreatment chamber 41 with
And heating chamber 42 all can use device of the prior art.
Bottom above-mentioned heating chamber 42, the end of conduit arranges a nozzle 43, and matrix material is sprayed to conveyer belt 33 from nozzle 43
Initiating terminal.
Further, the said equipment also includes that protective atmosphere processing means 5, above-mentioned protective atmosphere processing means 5 include protecting
Protect gas heating chamber 51 and atmosphere source chamber 50；
Above-mentioned atmosphere source chamber 50 connects above-mentioned protective gas heating chamber 51, and above-mentioned protective gas heating chamber 51 lower end arranges one
Conduit is passed through in above-mentioned main spray booth 30.Deposit protective atmosphere gas in atmosphere source chamber 50, this gas be noble gas, not with system
The protective gas of standby material reaction or can with prepare the reacting gas that material reacts.This protective atmosphere gas adds through protective gas
After the heating of hot cell 51, spraying process is protected to main spray booth 30 by transmission, is possible to prevent to prepare material oxidation.
Further, the said equipment also includes that carrier gas processing system 6, above-mentioned carrier gas processing system 6 include carrier gas room 60, remove
Oil device 62, dehydrater 61 and carrier gas heating chamber 63, above-mentioned carrier gas room 60, dehydrater 61, grease trap 62 and carrier gas heating chamber
63 are sequentially connected with, and above-mentioned carrier gas heating chamber 63 lower end arranges opening and connects the top of above-mentioned first Laval nozzle 21.At carrier gas
High pressure carrier gas in reason system 6 enters the first Laval nozzle 21 after treatment, through the acceleration of the first Laval nozzle 21, mixed
Close the atmosphere forming high velocity, low pressure in room 20, suck the mixture in thermal balance room, it is not necessary to use the equipment such as pump.Above-mentioned grease trap
62, dehydrater 61, carrier gas heating chamber 63 all can use existing equipment.
The gas-liquid biphase system provided in this utility model embodiment is for the equipment of powder body, and work process is: preheating cabinet and master
Add and raw material is heated to different physical state by hot tank, and mix in thermal balance room；Height in carrier gas processing system 6
Ballast gas enters the first Laval nozzle 21 after treatment, through the acceleration of the first Laval nozzle 21, is formed in mixing chamber 20
The atmosphere of high velocity, low pressure, sucks the mixture in thermal balance room；With carrier gas in mixture injection mixing chamber 20 in thermal balance room
Mixing, and under the effect of carrier gas, enter the second Laval nozzle 22, further speed up and be sprayed to the biography in main spray booth 30
Send on band 33；Meanwhile, matrix material is sprayed to the initiating terminal of conveyer belt 33 after pretreatment and the heating such as sieve, and transmits
Band 33 drive matrix material runs toward main spray booth 30；The material of the second Laval nozzle 22 ejection is sprayed to conveyer belt 33 matrix
On material, it is combined, obtains composite；Finally collect this composite by material collecting device again.
The gas-liquid biphase system provided in this utility model embodiment, for the equipment of powder body, uses electromagnetic wave transmitter auxiliary to add
Heat, activation, mixed raw material, on the basis of energy-saving and cost-reducing, and the material of metal or other indissolubles is heated to liquid,
Gaseous state, plasmoid, Supercritical Conditions, therefore, it can manufacture the multiple materials such as composition metal powder body material, Graphene
Material；The principle of application Laval nozzle high velocity, low pressure, raw material and high pressure carrier gas mix at mixing chamber, are conducive to the fastest
The mixing of speed, has saved the equipment such as pump；The use of Laval nozzle, can accelerate to velocity of sound by the highest for high pressure carrier gas, is conducive to
The material of high degree of dispersion different conditions, reaches the other mixed-scale of molecular level, sprays to conveyer belt and can obtain ultra-fine grain, table
Specific area is big, activity is high.Carrier gas, raw material, matrix material all can carry out pretreatment, it is ensured that the high-purity of powder body.
The foregoing is only preferred embodiment of the present utility model, not thereby limit the scope of the claims of the present utility model,
Every equivalent structure utilizing this utility model description and accompanying drawing content to be made or equivalence flow process conversion, or directly or indirectly transport
It is used in other relevant technical fields, is the most in like manner included in scope of patent protection of the present utility model.
Claims (10)
1. a gas-liquid biphase system is for the equipment of powder body, it is characterised in that include raw material annealing device, mixing arrangement and
Spray equipment；
Described mixing arrangement includes mixing chamber, the first Laval nozzle and the second Laval nozzle；The top of described mixing chamber
Running through and arrange described first Laval nozzle, the bottom of described mixing chamber connects described second Laval nozzle；Described second draws
Wa Er nozzle tip is passed through described spray equipment；
Described raw material annealing device is by the raw material mixing of different physical states, and connects described mixing arrangement by conduit
Mixing chamber.
2. gas-liquid biphase system as claimed in claim 1 is for the equipment of powder body, it is characterised in that described raw material annealing device
Hot tank and thermal balance case is added including preheating cabinet, master；Raw material is heated to liquid by described preheating cabinet, and described master adds hot tank by former
Material is heated to gaseous state；
Bottom described preheating cabinet and main heating bottom portion connects described thermal balance case, described thermal balance bottom by conduit respectively
Portion connects described mixing chamber by conduit.
3. gas-liquid biphase system as claimed in claim 2 is for the equipment of powder body, it is characterised in that described preheating cabinet includes the first case
Body, the first heating jacket and the first electromagnetic wave transmitter；Described main heating case include the second casing, the second heating jacket and
Second electromagnetic wave transmitter；Described thermal balance case includes the 3rd casing, the 3rd heating jacket and the 3rd electromagnetic wave transmitter；
Described first casing periphery arranges described first heating jacket, and described first box bottom connects the described 3rd by conduit
Casing, the bottom of described first casing differs from catheter position and arranges described first electromagnetic wave transmitter；Described second casing is peripheral
Arranging described second heating jacket, described second box bottom connects described 3rd casing by conduit, described second casing
Bottom differs from catheter position and arranges described second electromagnetic wave transmitter；The periphery of described 3rd casing arranges described 3rd heating folder
Set, the bottom sides of described 3rd casing connects described mixing chamber by conduit, and described 3rd box bottom arranges the described 3rd
Electromagnetic wave transmitter.
4. gas-liquid biphase system as claimed in claim 1 is for the equipment of powder body, it is characterised in that described mixing arrangement also includes the
Four heating jackets, described 4th heating jacket is coated on described mixing chamber, the first Laval nozzle and the second Laval nozzle
Periphery, and the top of described 4th heating jacket and bottom be correspondingly arranged on fixing described first Laval nozzle and second and draw
The opening of Wa Er jet pipe.
5. gas-liquid biphase system as claimed in claim 1 is for the equipment of powder body, it is characterised in that described spray equipment includes spraying
Room, arranges conveyer belt, main spray booth and powder thickness actuator in described spray booth；
Described main spray booth is arranged in the middle part of described spray booth, and described main jet is coated with ceiling portion and is provided with for described second Lavalle spray
The opening that pipe end is passed through, described main jet is coated with the lower section of indoor second Laval nozzle end and arranges described conveyer belt；Described biography
The one end sending band is provided above described powder thickness actuator, and described powder thickness actuator is fixed on described main spray booth side
Bottom, and and described conveyer belt between set the thickness of material layer on clearance control conveyer belt.
6. gas-liquid biphase system as claimed in claim 5 is for the equipment of powder body, it is characterised in that described spray equipment also includes heat
Exchanger；
Described heat exchanger is arranged in described conveyer belt internal voids and carries out heat exchange with the material on its upper conveyor.
7. gas-liquid biphase system as claimed in claim 5 is for the equipment of powder body, it is characterised in that described spray equipment also includes receiving
Material device；Described material collecting device includes conveyor belt cleaner, powder body collecting chamber and vibrating screen panel；
Described conveyer belt transmits end and connects described powder body collecting chamber, and is provided with described conveyor belt cleaner cleaning conveyer belt；
Described powder body collecting chamber lower end is provided with opening and houses described vibrating screen panel；Described vibrating screen panel includes screen cloth and vibrations horse
Reaching, described vibrations motor drives the vibrations of described screen cloth.
8. gas-liquid biphase system as claimed in claim 5 is for the equipment of powder body, it is characterised in that described equipment also includes matrix material
Material discharging device, described matrix material discharging device includes pretreatment chamber and heating chamber；Add described in the connection of described pretreatment chamber
Hot cell, arranges a conduit and is passed through in described spray booth, and be positioned at above the initiating terminal of described conveyer belt bottom described heating chamber；
Bottom described heating chamber, the end of conduit arranges a nozzle.
9. gas-liquid biphase system as claimed in claim 5 is for the equipment of powder body, it is characterised in that described equipment also includes protecting gas
Atmosphere processing means, described protective atmosphere processing means includes protective gas heating chamber and atmosphere source chamber；
Described atmosphere source chamber connects described protective gas heating chamber, and described protective gas heating chamber lower end arranges a conduit and is passed through institute
State main jet and be coated with indoor.
10. the gas-liquid biphase system as described in claim 1 or 4 is for the equipment of powder body, it is characterised in that described equipment also includes carrying
Gas processing system, described carrier gas processing system includes carrier gas room, grease trap, dehydrater and carrier gas heating chamber, described carrier gas room,
Dehydrater, grease trap and carrier gas heating chamber are sequentially connected with, and described carrier gas heating chamber lower end arranges opening connection described first and draws
The top of Wa Er jet pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620736248.9U CN205850788U (en) | 2016-07-13 | 2016-07-13 | Gas-liquid biphase system is for the equipment of powder body |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620736248.9U CN205850788U (en) | 2016-07-13 | 2016-07-13 | Gas-liquid biphase system is for the equipment of powder body |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205850788U true CN205850788U (en) | 2017-01-04 |
Family
ID=57647069
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620736248.9U Expired - Fee Related CN205850788U (en) | 2016-07-13 | 2016-07-13 | Gas-liquid biphase system is for the equipment of powder body |
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| Country | Link |
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| CN (1) | CN205850788U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106000227A (en) * | 2016-07-13 | 2016-10-12 | 张启辉 | System for preparing powder with gas phase and liquid phase |
-
2016
- 2016-07-13 CN CN201620736248.9U patent/CN205850788U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106000227A (en) * | 2016-07-13 | 2016-10-12 | 张启辉 | System for preparing powder with gas phase and liquid phase |
| WO2018010584A1 (en) * | 2016-07-13 | 2018-01-18 | 深圳市知赢科技有限公司 | System for preparing powder by means of gas phase and liquid phase |
| CN106000227B (en) * | 2016-07-13 | 2019-01-25 | 深圳市航盛新材料技术有限公司 | Gas-liquid biphase system for powder system |
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