CN208990754U - A kind of continuous spray granulator - Google Patents
A kind of continuous spray granulator Download PDFInfo
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- CN208990754U CN208990754U CN201821330181.4U CN201821330181U CN208990754U CN 208990754 U CN208990754 U CN 208990754U CN 201821330181 U CN201821330181 U CN 201821330181U CN 208990754 U CN208990754 U CN 208990754U
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- hot wind
- cloth bag
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Abstract
The utility model discloses a kind of continuous spray granulators, belong to drying device field, it is more uniform to be intended to provide a kind of powder granule for making to be formed after granulation, improve the continuous spray granulator of the final product quality of material, hopper is directly fallen into material after solution granulation not sieved, it will lead to the problem of powder granule size unevenness, its drip irrigation device is as follows, it includes rack, dust trapping chamber is successively arranged in rack from top to bottom, granulating chamber, spray chamber and hot wind mixing chamber, trapping filter mechanism is equipped in dust trapping chamber, air outlet is equipped on the upside of dust trapping chamber, air outlet is communicated with exhaust fan, spray chamber's side wall is equipped with spray assemblies, the side wall of hot wind mixing chamber is equipped with hot wind inlet；Spray chamber lower end is equipped with the air inducing net that hot wind supply passes through, and is equipped with material blanking tube in the middle part of air inducing net, one end of material blanking tube is connected to spray chamber, and the other end is communicated with discharge bucket.The utility model is suitable for the drying and granulating of food and drug.
Description
Technical field
The utility model relates to a kind of granulator, in particular to a kind of continuous spray granulator.
Background technique
Granular material has good mobility and gas permeability, while having easy to maintain, soluble and being unlikely to deteriorate
Advantage, therefore, grain products are widely used in the various catalyst and additive, medicine of foodstuff instant drink, chemical
Granulation before the various electuary medicines of class, tabletting and the granulation before the various forming ceramics of building material etc., especially current porcelain
The new method of brick production is all to suppress to carry out molding technique again after using granulation.It can be seen that powder granulation is food, changes
The indispensable production technology of the numerous products of the industries such as work, medicine, building materials, metallurgy, agricultural, military project and refractory material.
Notification number is that the Chinese patent of CN206081081U discloses a kind of one-step-granulating method, including rack, tank body, hot wind
Module, spraying granulation module and grain module out, the rack are equipped with one group of installation long hole, and the tank body is by peg installs in machine
It at one group of installation long hole on frame, and can vertically move up and down, the tank body is equipped with hot air chamber and spray chamber, bottom
Equipped with air inlet, top is equipped with gas outlet, and the hot wind module includes air-heater, hot air pipe and filter, the hot air pipe
One end is communicated by filter with the hot-blast outlet of air-heater.
Although this one-step-granulating method can pelletize to material, granulation after material directly fall into hopper not into
Row screening will lead to powder granule size unevenness, influence the final product quality of material.
Utility model content
The purpose of the utility model is to provide a kind of continuous spray granulators, have the powder granule for making to be formed after granulation more
The advantages of adding uniformly, improving the final product quality of material.
The above-mentioned technical purpose of the utility model has the technical scheme that
A kind of continuous spray granulator, including rack, be successively arranged in the rack from top to bottom dust trapping chamber, granulating chamber,
Spray chamber and hot wind mixing chamber are equipped with trapping filter mechanism in the dust trapping chamber, are equipped with air outlet, institute on the upside of the dust trapping chamber
It states air outlet and is communicated with exhaust fan, spray chamber's side wall is equipped with spray assemblies, and the side wall of the hot wind mixing chamber is equipped with hot wind
Import；
The spray chamber lower end is equipped with the air inducing net that hot wind supply passes through, and material blanking tube is equipped in the middle part of the air inducing net, described to fall
One end of expects pipe is connected to spray chamber, and the other end is communicated with discharge bucket.
By using above-mentioned technical proposal, wet stock is sprayed into spray chamber by spray assemblies, constantly has heat in hot wind mixing chamber
Ascension on wind direction, with quick heat exchange, wet stock, which is realized, to be separated by solid-liquid separation, and exhaust fan extracts vapor by air outlet out,
Dust trapping chamber is set to form negative pressure, powder granule is captured cloth bag trapping, makes to be attached to the powder on trapping cloth bag by pulse components
Particles sink carries out again gluing with wet stock and is granulated, keep powder granule increasing, until powder during sinking
The self weight of body particle is greater than upward wind-force, and powder granule drops to material blanking tube under the effect of gravity, then, dry powder
Grain enters discharge bucket by material blanking tube.The powder granule of discharge is sieved in the setting of material blanking tube, can be excessive by diameter
Powder granule is screened out, due to powder granule blanking rely on self gravity, the too small particle of diameter due to its own gravity compared with
It is small, it will continue to upward ascension in the environment of hot wind and negative pressure and be granulated, until reaching the standard of discharging.
Further, the length of the material blanking tube is the total height of dust trapping chamber, granulating chamber, spray chamber and hot wind mixing chamber
A quarter to one third.
By using above-mentioned technical proposal, if the length of material blanking tube is too short, powder granule can be blocked up due to having little time discharging
Material blanking tube is filled in, the normal use of continuous spray granulator is influenced；If the length of material blanking tube is too long, understands wasting space and can extend
Discharging time reduces production efficiency.The length of material blanking tube is total height of dust trapping chamber, granulating chamber, spray chamber and hot wind mixing chamber
For a quarter of degree to one third, this unique design can either reduce a possibility that material blanking tube is blocked, and can mention
The discharging efficiency of high powder granule.
Further, the trapping filter mechanism includes trapping component and pulse components；
The trapping component includes mounting plate and several trapping cloth bags, and the mounting plate is fixedly installed on the side of dust trapping chamber
Wall, Circle-Array shows several circular mounting holes on the mounting plate, and the sacks of several trapping cloth bags pass through elastic expansion ring
It is fixed on mounting plate.
By using above-mentioned technical proposal, the powder granule formed after granulating chamber is pelletized the cloth bag that is captured is trapped,
Make powder be not easy to escape and go out from air outlet, can be improved the mass output rate of powder granule.
Further, it is equipped with the cloth bag frame being adapted to trapping cloth bag in the trapping cloth bag, if the cloth bag frame includes
The both ends of Heavenly Stems and Earthly Branches strut, the cloth bag frame have been respectively fixedly connected with set frame.
By using above-mentioned technical proposal, cloth bag frame is used to support trapping cloth bag, makes to trap cloth bag during the work time not
It easily deforms, is not easy to wind with the trapping cloth bag of surrounding；Set frame can make cloth bag frame be easier to be inserted in cloth bag.
Further, the pulse components include gas bag, electromagnetic impulse valve and injection tube, and the gas bag is located at dust trapping chamber
It is fixedly connected outside and with dust trapping chamber, one end of the injection tube is located in dust trapping chamber, and the other end is pierced by dust trapping chamber and passes through electromagnetism
Pulse valve is connected to gas bag, and the injection tube lower end is provided with blowing mouth.
It is being caught after trapping powder granule trapping a period of time that cloth bag forms granulation by using above-mentioned technical proposal
The outer wall of collection cloth bag is attached with more powder granule, must be purged the powder granule of cloth bag surface, using pulse components
Trapping cloth bag is blown, electromagnetic impulse valve is opened by controller, and the compressed air in gas bag enters injection tube, passes through blowing
Mouth directive traps cloth bag center, and the powder granule for trapping cloth bag outer wall is shaken off, and improves the arresting efficiency of trapping cloth bag.Blowing
Mouth can make to be blown into air flow collection in trapping cloth bag, and be sufficiently blown to trapping cloth bag, and the powder for trapping cloth bag surface is made
Particle is fallen as much as possible, to play the role of good cleaning.
Further, the spray assemblies include several high-pressure atomization spray heads, the high-pressure atomization spray head circumference array in
Spray chamber's side wall；
The high-pressure atomization spray head is equipped with negative throat noz(zle), and the discharge port of the negative throat noz(zle) is arranged upward.
By using above-mentioned technical proposal, it is in droplet shape when high-pressure atomization spray head ejects wet stock, makes to pelletize
The powder granule formed afterwards is more anxious fine and smooth uniform.
Further, the granulating chamber is in reverse frustoconic, and the incline of the granulating chamber and the angle of axis are 15 ° to 30 °.
By using above-mentioned technical proposal, the incline of granulating chamber and the angle of axis are 15 ° to 30 °, advantageously reduce powder
Residual of the body particle in granulating chamber side wall.
Further, the granulating chamber side wall is equipped with observation window.
By using above-mentioned technical proposal, observation window facilitates look at the indoor granulation situation of granulation, without shutting down, operation
It is convenient.
In conclusion the utility model has the following beneficial effects:
1. using material blanking tube, reach and the powder granule of discharge has been sieved, has made the powder granule formed after granulation
It is more uniform, improve the effect of the final product quality of material；
2. due to four points of the total height that the length of material blanking tube is dust trapping chamber, granulating chamber, spray chamber and hot wind mixing chamber
One of to one third unique design, a possibility that material blanking tube is blocked can either be reduced, and can be improved powder granule
Discharge efficiency.
Detailed description of the invention
Fig. 1 is to show in the present embodiment for embodying the positional relationship of dust trapping chamber, granulating chamber, spray chamber and hot wind mixing chamber
It is intended to；
Fig. 2 is in the present embodiment for embodying the connection relationship diagram between trapping component and each component of pulse components；
Fig. 3 is in the present embodiment for embodying the structural schematic diagram of cloth bag frame.
In figure, 1, rack；2, dust trapping chamber；21, air outlet；211, exhaust fan；3, granulating chamber；31, observation window；4, spraying
Room；41, spray assemblies；411, high-pressure atomization spray head；4111, negative throat noz(zle)；42, air inducing net；421, material blanking tube；5, hot wind mixes
Room；51, hot wind inlet；6, discharge bucket；7, component is trapped；71, mounting plate；711, mounting hole；72, cloth bag is trapped；721, cloth bag
Frame；7211, support rod；7212, frame is covered；8, pulse components；81, gas bag；82, electromagnetic impulse valve；83, injection tube；831, it is blown
Mouth.
Specific embodiment
The utility model is described in further detail below in conjunction with attached drawing.
Wherein identical components are presented with like reference characters.It should be noted that word used in the following description
Language "front", "rear", "left", "right", "up" and "down" refer to the direction in attached drawing, word " bottom surface " and " top surface ", "inner" and
"outside" refers respectively to the direction towards or away from geometric center of specific component.
A kind of continuous spray granulator is successively arranged dust trapping chamber in rack 1 as shown in Figure 1, including rack 1 from top to bottom
2, granulating chamber 3, spray chamber 4 and hot wind mixing chamber 5, air outlet 21 is equipped on the upside of dust trapping chamber 2, and air outlet 21 is communicated with exhaust fan
211,3 side wall of granulating chamber is equipped with observation window 31, and trapping filter mechanism is equipped in dust trapping chamber 2.
As shown in Fig. 2, trapping filter mechanism includes trapping component 7 and pulse components 8, trapping component 7 includes mounting plate 71
With several trapping cloth bags 72, mounting plate 71 is fixedly installed on the side wall of dust trapping chamber 2, and Circle-Array shows several circles on mounting plate 71
Mounting hole 711, it is several trapping cloth bags 72 sacks be fixed on mounting plate 71 by elastic expansion ring.After the granulation of granulating chamber 3
The powder granule of the formation cloth bag 72 that is captured is trapped, and is made powder be not easy to escape and go out from air outlet 21, be can be improved powder
The mass output rate of particle.
As shown in figure 3, trapping cloth bag 72(is referring to fig. 2) in be equipped with and trap the cloth bag frame 721 that is adapted to of cloth bag 72, cloth bag
Frame 721 includes several support rods 7211, and the both ends of cloth bag frame 721 have been respectively fixedly connected with set frame 7212.Cloth bag frame 721 is for branch
Support trapping cloth bag 72, makes trapping cloth bag 72 be not susceptible to deform during the work time, is not easy and the trapping cloth bag 72 of surrounding occurs
Winding；Set frame 7212 can make cloth bag frame 721 be easier to be inserted in cloth bag.
As shown in Fig. 2, pulse components 8 include gas bag 81, electromagnetic impulse valve 82 and injection tube 83, gas bag 81 is located at trapping
Room 2 is outer and is fixedly connected with dust trapping chamber 2, and one end of injection tube 83 is located in dust trapping chamber 2, and the other end is pierced by dust trapping chamber 2 and passes through
Electromagnetic impulse valve 82 is connected to gas bag 81, and 83 lower end of injection tube is provided with blowing mouth 831.The powder that 72 pairs of cloth bag granulations of trapping are formed
Body granule capturing for a period of time after, trapping cloth bag 72 outer wall be attached with more powder granule, must be by the powder of cloth bag surface
Body particle is purged, and is blown using 8 pairs of trapping cloth bags 72 of pulse components, electromagnetic impulse valve 82 is opened by controller, gas
Compressed air in packet 81 enters injection tube 83, traps 72 center of cloth bag by blowing 831 directive of mouth, will trap 72 outer wall of cloth bag
Powder granule shake off, improve trapping cloth bag 72 arresting efficiency.Blowing mouth 831 can make to be blown into trapping cloth bag in air flow collection
In 72, and trapping cloth bag 72 is sufficiently blown, falls the powder granule for trapping 72 surface of cloth bag as much as possible, to rise
It is acted on to good cleaning.
As shown in Fig. 2, 4 side wall of spray chamber is equipped with spray assemblies 41, spray assemblies 41 include several high-pressure atomization spray heads
411,411 circumference array of high-pressure atomization spray head is in 4 side wall of spray chamber.High-pressure atomization spray head 411 is equipped with negative throat noz(zle) 4111, gradually
The discharge port of contracting nozzle 4111 is arranged upward.4 lower end of spray chamber is equipped with the air inducing net 42 that hot wind supply passes through, and sets in the middle part of air inducing net 42
There is material blanking tube 421, material blanking tube 421 is located in hot wind mixing chamber 5, and one end of material blanking tube 421 is connected to spray chamber 4, and the other end connects
It is connected with discharge bucket 6.The side wall of hot wind mixing chamber 5 is equipped with the hot wind inlet 51 for wet stock to be dried.Spray assemblies 41
Wet stock is sprayed into spray chamber 4, constantly has the upward ascension of hot wind in hot wind mixing chamber 5, with quick heat exchange, wet stock is real
It is now separated by solid-liquid separation, exhaust fan 211 extracts vapor by air outlet 21 out, and dust trapping chamber 2 is made to form negative pressure, and powder granule is captured
Cloth bag 72 traps, and so that the powder granule being attached on trapping cloth bag 72 is sunk by pulse components 8, during sinking, with
Wet stock carries out again gluing and is granulated, and keeps powder granule increasing, until the self weight of powder granule is greater than upward wind-force,
Powder granule drops to material blanking tube 421 under the effect of gravity, and then, dry powder granule enters discharging by material blanking tube 421
Bucket 6.The powder granule of discharge is sieved in the setting of material blanking tube 421, can sieve the excessive powder granule of diameter
It removes, since powder granule blanking relies on self gravity, the too small particle of diameter is since its own gravity is smaller, in hot wind and negative pressure
In the environment of will continue to upward ascension and be granulated, until reaching the standard of discharging.
As shown in Fig. 2, powder granule can block material blanking tube due to having little time discharging if the length of material blanking tube 421 is too short
421, influence the normal use of continuous spray granulator；If the length of material blanking tube 421 is too long, understands wasting space and can extend out
Expect the time, reduces production efficiency.Therefore, the length of material blanking tube 421 is set as dust trapping chamber 2, granulating chamber 3, spray chamber 4 and hot wind
For a quarter of the total height of mixing chamber 5 to one third, this unique design can either reduce what material blanking tube 421 was blocked
Possibility, and can be improved the discharging efficiency of powder granule.
As shown in Figure 1, granulating chamber 3 is in reverse frustoconic, the incline of granulating chamber 3 and the angle of axis are 15 ° to 30 °, this
Design advantageously reduces powder granule in the residual of 3 side wall of granulating chamber.
Specific implementation process: go out to be continually fed into hot wind in hot wind inlet 51, wet stock is become small by high-pressure atomization spray head 411
Spray chamber 4 is sprayed into after drop, droplet is with the upward ascension of hot wind, and with quick heat exchange, wet stock, which is realized, to be separated by solid-liquid separation,
Exhaust fan 211 extracts vapor by air outlet 21 out, and dust trapping chamber 2 is made to form negative pressure.
Powder granule be captured cloth bag 72 trapping, by 8 timing of pulse components to trapping cloth bag 72 be blown, make to adhere to
Powder granule on trapping cloth bag 72 sinks.Electromagnetic impulse valve 82 is opened by controller, and the compressed air in gas bag 81 enters
Injection tube 83 traps 72 center of cloth bag by blowing 831 directive of mouth, the powder granule for trapping 72 outer wall of cloth bag is shaken off.
During sinking, gluing is carried out again with wet stock and is granulated, keeps powder granule increasing, until powder
The self weight of particle is greater than upward wind-force, and powder granule drops to material blanking tube 421 under the effect of gravity, then, dry powder
Particle enters discharge bucket 6 by material blanking tube 421.
This specific embodiment is only the explanation to the utility model, is not limitations of the present invention, ability
Field technique personnel can according to need the modification that not creative contribution is made to the present embodiment after reading this specification, but
As long as all by the protection of Patent Law in the scope of the claims of the utility model.
Claims (8)
1. a kind of continuous spray granulator, including rack (1), catch it is characterized in that: being successively arranged from top to bottom in the rack (1)
Collect room (2), granulating chamber (3), spray chamber (4) and hot wind mixing chamber (5), trapping filter mechanism be equipped in the dust trapping chamber (2),
Air outlet (21) are equipped on the upside of the dust trapping chamber (2), the air outlet (21) is communicated with exhaust fan (211), the spray chamber (4)
Side wall is equipped with spray assemblies (41), and the side wall of the hot wind mixing chamber (5) is equipped with hot wind inlet (51)；
Spray chamber (4) lower end is equipped with the air inducing net (42) that hot wind supply passes through, and is equipped with material blanking tube in the middle part of the air inducing net (42)
(421), one end of the material blanking tube (421) is connected to spray chamber (4), and the other end is communicated with discharge bucket (6).
2. a kind of continuous spray granulator according to claim 1, it is characterized in that: the length of the material blanking tube (421) is
Dust trapping chamber (2), granulating chamber (3), spray chamber (4) and hot wind mixing chamber (5) total height a quarter to one third.
3. a kind of continuous spray granulator according to claim 1, it is characterized in that: the trapping filter mechanism includes trapping
Component (7) and pulse components (8)；
The trapping component (7) includes mounting plate (71) and several trapping cloth bags (72), and the mounting plate (71) is fixedly installed on
The side wall of dust trapping chamber (2), Circle-Array shows several circular mounting holes (711), several trappings on the mounting plate (71)
The sack of cloth bag (72) is fixed on mounting plate (71) by elastic expansion ring.
4. a kind of continuous spray granulator according to claim 3, it is characterized in that: being equipped in the trapping cloth bag (72)
The cloth bag frame (721) being adapted to trapping cloth bag (72), the cloth bag frame (721) includes several support rods (7211), the cloth bag
The both ends of frame (721) have been respectively fixedly connected with set frame (7212).
5. a kind of continuous spray granulator according to claim 4, it is characterized in that: the pulse components (8) include gas bag
(81), electromagnetic impulse valve (82) and injection tube (83), the gas bag (81) are located at dust trapping chamber (2) outside and consolidate with dust trapping chamber (2)
Fixed connection, one end of the injection tube (83) are located in dust trapping chamber (2), and the other end is pierced by dust trapping chamber (2) and passes through electromagnetic pulse
Valve (82) is connected to gas bag (81), and injection tube (83) lower end is provided with blowing mouth (831).
6. a kind of continuous spray granulator according to claim 5, it is characterized in that: the spray assemblies (41) include several
High-pressure atomization spray head (411), high-pressure atomization spray head (411) circumference array is in spray chamber (4) side wall；
The high-pressure atomization spray head (411) is equipped with negative throat noz(zle) (4111), and the discharge port of the negative throat noz(zle) (4111) is upward
Setting.
7. a kind of continuous spray granulator according to claim 6, it is characterized in that: the granulating chamber (3) is in reverse frustoconic,
The incline of the granulating chamber (3) and the angle of axis are 15 ° to 30 °.
8. a kind of continuous spray granulator according to claim 7 is seen it is characterized in that: the granulating chamber (3) side wall is equipped with
Examine window (31).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821330181.4U CN208990754U (en) | 2018-08-16 | 2018-08-16 | A kind of continuous spray granulator |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821330181.4U CN208990754U (en) | 2018-08-16 | 2018-08-16 | A kind of continuous spray granulator |
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| Publication Number | Publication Date |
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| CN208990754U true CN208990754U (en) | 2019-06-18 |
Family
ID=66798575
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| CN201821330181.4U Active CN208990754U (en) | 2018-08-16 | 2018-08-16 | A kind of continuous spray granulator |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112897990A (en) * | 2021-03-05 | 2021-06-04 | 株洲火炬安泰新材料有限公司 | Centrifugal spray granulation process for preparing high-density ITO target |
| CN114620770A (en) * | 2022-05-07 | 2022-06-14 | 长江师范学院 | Granulation impurity removal method for negative electrode material of spheroidal powder lithium iron oxide ion battery |
| CN114684862A (en) * | 2022-05-07 | 2022-07-01 | 长江师范学院 | Treatment method of lithium ion battery cathode material |
-
2018
- 2018-08-16 CN CN201821330181.4U patent/CN208990754U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112897990A (en) * | 2021-03-05 | 2021-06-04 | 株洲火炬安泰新材料有限公司 | Centrifugal spray granulation process for preparing high-density ITO target |
| CN112897990B (en) * | 2021-03-05 | 2022-05-10 | 株洲火炬安泰新材料有限公司 | Centrifugal spray granulation process for preparing high-density ITO target |
| CN114620770A (en) * | 2022-05-07 | 2022-06-14 | 长江师范学院 | Granulation impurity removal method for negative electrode material of spheroidal powder lithium iron oxide ion battery |
| CN114684862A (en) * | 2022-05-07 | 2022-07-01 | 长江师范学院 | Treatment method of lithium ion battery cathode material |
| CN114620770B (en) * | 2022-05-07 | 2024-05-28 | 长江师范学院 | Granulating and impurity removing method for anode material of spheroidal powder ferric oxide lithium ion battery |
| CN114684862B (en) * | 2022-05-07 | 2024-05-28 | 长江师范学院 | Method for processing lithium ion battery cathode material |
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