CN206853625U - A kind of ultrafine powder Squeezinggranulator - Google Patents

A kind of ultrafine powder Squeezinggranulator Download PDF

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Publication number
CN206853625U
CN206853625U CN201720314271.3U CN201720314271U CN206853625U CN 206853625 U CN206853625 U CN 206853625U CN 201720314271 U CN201720314271 U CN 201720314271U CN 206853625 U CN206853625 U CN 206853625U
Authority
CN
China
Prior art keywords
mixing
frame
batch mixing
atomization
housing
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
Application number
CN201720314271.3U
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Chinese (zh)
Inventor
王记生
张彩霞
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangdong Dixingwei Industrial Co ltd
Foshan University
Original Assignee
Foshan Dili Granville Automation Equipment Co Ltd
Foshan University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Foshan Dili Granville Automation Equipment Co Ltd, Foshan University filed Critical Foshan Dili Granville Automation Equipment Co Ltd
Priority to CN201720314271.3U priority Critical patent/CN206853625U/en
Application granted granted Critical
Publication of CN206853625U publication Critical patent/CN206853625U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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  • Formation And Processing Of Food Products (AREA)

Abstract

It the utility model is related to a kind of ultrafine powder Squeezinggranulator; including frame, drive device, motor rack, batch mixing frame, granulation frame, mixing device, prilling granulator; motor rack, batch mixing frame are respectively arranged with the frame and is granulated frame; drive device is provided with the motor rack; the drive device is connected with the mixing device; the mixing device is connected by shaft coupling with prilling granulator, and described prilling granulator one end is provided with discharging sieve plate, and multigroup sieve aperture is provided with the discharging sieve plate;The utility model by being molded immediately after batch mixing; reduce trafficking step; by mixing atomization moisture in batch mixing, discharge after abundant batch mixing stirring, added immediately in comminutor housing after discharging; by the synergy for driving pelletizing drum and driven pelletizing drum; whole granulation process is completed, avoids and the problem of causing comminutor inner body service life of moisture is directly mixed in comminutor, simultaneously; middle batch mixing transportation is saved, accelerates the granulating and forming time.

Description

A kind of ultrafine powder Squeezinggranulator
Technical field
It the utility model is related to comminutor technical field, more particularly to a kind of ultrafine powder Squeezinggranulator.
Background technology
Ultrafine powder refers to that particle diameter is thinner less than 1 μm of powdered substance aluminum oxide grain sizes, and its sintering temperature is got over Therefore, high-purity super fine alumina has excellent sintering character and performance to low, while is also to prepare dispersion-strengtherning material The aggregate of many single ultramicro powders of good disperse phase of material is known as Ultramicro-powder Ultramicro-powders and (measured with its " bulk effect " Sonization effect) and " skin effect " be substantially distinguished from general particle and traditional block materials and turn into a kind of new shape existing for material State;
Ultrafine powder typically selects granulating and forming in processing and forming, and needs moisture during ultra-micro powder granulating and forming Addition with mixing, this mixed process can not be separated and carried out, and this moisture be infiltrated in prilling granulator, can influence to be granulated rolling The service life of cylinder, the particle that this mode is molded also have the uneven phenomenon of size.
The content of the invention
The utility model overcomes above-mentioned the deficiencies in the prior art, there is provided a kind of ultrafine powder Squeezinggranulator.This reality With new by being molded immediately after batch mixing, trafficking step is reduced, by mixing atomization moisture in batch mixing, is gone out after abundant batch mixing stirring Material, adds in comminutor housing, by driving the synergy of pelletizing drum and driven pelletizing drum, and passes through immediately after discharging Granulation groove in driving, driven pelletizing drum, the particle made is transported by tilting blanking plate to discharging sieve plate, until that will accord with The shaped granule for closing slot size sifts out, and completes whole granulation process, avoids and causing for moisture is directly mixed in comminutor The problem of comminutor inner body service life, meanwhile, middle batch mixing transportation is saved, accelerates the granulating and forming time.
The technical solution of the utility model:
A kind of ultrafine powder Squeezinggranulator, including frame, drive device, motor rack, batch mixing frame, granulation frame, batch mixing dress Put, prilling granulator, motor rack, batch mixing frame are respectively arranged with the frame and is granulated frame, driving is provided with the motor rack Device, the drive device are connected with the mixing device, and the mixing device is connected by shaft coupling with prilling granulator, described Prilling granulator one end is provided with discharging sieve plate, and multigroup sieve aperture is provided with the discharging sieve plate;
The drive device includes motor, and the motor is fixedly mounted on the motor rack, the driving Electric machine main shaft is fixedly connected with the driving pulley, and the driving pulley is connected by driving belt with driven pulley, it is described from Movable belt pulley is fixedly connected by connecting shaft with the mixing device;
The mixing device includes mixing roller, and the mixing roller is fixedly mounted on the batch mixing frame, the batch mixing Batch mixing main shaft is provided with roller, described batch mixing main shaft one end is fixedly connected with the driven pulley, and the batch mixing main shaft is another End is connected by shaft coupling with the prilling granulator, is additionally provided with batch mixing flabellum on the batch mixing main shaft, in the mixing roller It is additionally provided with water atomization plant;
The prilling granulator includes comminutor housing, and the comminutor housing is fixedly mounted on the granulation frame, described Be provided with driving pelletizing drum and driven pelletizing drum in comminutor housing, the driving pelletizing drum main shaft by shaft coupling with The batch mixing main shaft is fixedly connected, and multigroup granulation groove is machined with respectively on the driving pelletizing drum, the driven pelletizing drum, Inclination blanking plate is provided with the comminutor housing, the blanking plate lower is connected in the discharging sieve plate, the discharging Sieve plate is fixedly mounted in the frame.
Preferably, charging aperture, discharging opening and atomization mouth, the discharging opening are machined with the mixing roller respectively to be arranged on The mixing roller bottom, the atomization mouth are provided with the water atomization plant.
Preferably, the water atomization plant includes atomization housing, and atomization water tank, the mist are provided with the atomization housing Change water tank to be connected with the atomization housing by pipeline, ultrasonic atomization piece is set in the atomization housing.
Preferably, the driving pulley, the driven pulley outer end are respectively arranged with belt wheel protective cover.
The utility model has the advantages that relative to prior art:
Ultrafine powder Squeezinggranulator disclosed in the utility model reduces trafficking step, led to by being molded immediately after batch mixing Cross in batch mixing and mix atomization moisture, the moisture of the ratio calculated is added in water tank, is added in mixing roller and calculates Ultramicro-powder The quality of body, open check valve, after the moisture of fixed amount is fully atomized, the water after atomization is mixed with ultra micro powder, fully Discharge, added immediately in comminutor housing after discharging, by the association for driving pelletizing drum and driven pelletizing drum after batch mixing stirring Same-action, and by the granulation groove on driving, driven pelletizing drum, by the particle made by tilting blanking plate to discharging sieve plate Transport, sifts out until by the shaped granule for meeting slot size, completes whole granulation process, avoids and is mixed directly in comminutor Add the problem of causing comminutor inner body service life of moisture, meanwhile, middle batch mixing transportation is saved, accelerates and makes Grain molding time;
The utility model by discharge sieve plate sieve material, the particle of general size is sifted out, bulky grain is extruded again until Meet the requirements.
Additional aspect and advantage of the present utility model will be set forth in part in the description, partly by from following description In become obvious, or recognized by the practice of invention.
Brief description of the drawings
Fig. 1 is dimensional structure diagram of the present utility model;
Fig. 2 is top view of the present utility model;
Fig. 3 is front view of the present utility model;
Fig. 4 is the utility model left view;
Fig. 5 is the structural representation of stopper one in the utility model;
Fig. 6 is the internal structure schematic diagram of stopper in the utility model.
1- frames in figure;2- drive devices;3- motor racks;4- batch mixing framves;5- is granulated frame;6- mixing devices;7- is granulated dress Put;8- shaft couplings;9- discharging sieve plates;10- sieve apertures;11- motors;12- driving pulleys;13- driven pulleys;14- batch mixings roll Cylinder;15- batch mixing main shafts;16- batch mixing flabellums;17- drives pelletizing drum;The driven pelletizing drums of 18-;19- is granulated groove;20- is fed Mouthful;21- discharging openings;22- is atomized mouth;23- is atomized housing;24- is atomized water tank;25- drainage pipelines;26- ultrasonic atomization pieces; 27- check valves;28- belt wheel protective covers;29- charge doors.
Embodiment
The utility model is described in detail below with reference to accompanying drawing.
With reference to shown in Fig. 1 to Fig. 6, a kind of ultrafine powder Squeezinggranulator disclosed in the present embodiment, including frame 1, driving Device 2, motor rack 3, batch mixing frame 4, frame 5, mixing device 6, prilling granulator 7 are granulated, are respectively arranged with motor rack in the frame 1 3rd, batch mixing frame 4 and frame 5 is granulated, drive device 2, the drive device 2 and the mixing device 6 is provided with the motor rack 3 Connection, the mixing device 6 are connected by shaft coupling 8 with prilling granulator 7, and described one end of prilling granulator 7 is provided with discharging sieve plate 9, it is described discharging sieve plate 9 on be provided with multigroup sieve aperture 10;
The drive device 2 includes motor 11, and the motor 11 is fixedly mounted on the motor rack 3, institute State the main shaft of motor 11 to be fixedly connected with the driving pulley 12, the driving pulley 12 passes through driving belt and driven pulley 13 connections, the driven pulley 13 are fixedly connected by connecting shaft with the mixing device 6;
The mixing device 6 includes mixing roller 14, and the mixing roller 14 is fixedly mounted on the batch mixing frame 4, institute State and batch mixing main shaft 15 is provided with mixing roller 14, described one end of batch mixing main shaft 15 is fixedly connected with the driven pulley 13, institute State the other end of batch mixing main shaft 15 to be connected with the prilling granulator 7 by shaft coupling 8, batch mixing is additionally provided with the batch mixing main shaft 15 Flabellum 16, water atomization plant is additionally provided with the mixing roller 14;
The prilling granulator 7 includes comminutor housing, and the comminutor housing is fixedly mounted on the granulation frame 5, institute State and driving pelletizing drum 17 and driven pelletizing drum 18 are provided with comminutor housing, the driving main shaft of pelletizing drum 17 passes through Shaft coupling 8 is fixedly connected with the batch mixing main shaft 15, is added respectively on the driving pelletizing drum 17, the driven pelletizing drum 18 Work has multigroup granulation groove 19, is provided with inclination blanking plate in the comminutor housing, the blanking plate lower in the discharging Sieve plate 9 is connected, and the discharging sieve plate 9 is fixedly mounted in the frame 1, and charge door 29 is provided with the comminutor housing.
Specifically, charging aperture 20, discharging opening 21 and atomization mouth 22, the discharging are machined with the mixing roller 14 respectively Mouth 21 is arranged on the bottom of mixing roller 14, and the atomization mouth 22 is provided with the water atomization plant.
Specifically, the water atomization plant includes atomization housing 23, atomization water tank 24 is provided with the atomization housing 23, The atomization water tank 24 is connected by drainage pipeline 25 with the atomization housing 23, and ultrasonic fog is set in the atomization housing 23 Change piece 26.
Specifically, check valve 27 is provided with the drainage pipeline.
Specifically, the driving pulley 12, the outer end of the driven pulley 13 are respectively arranged with belt wheel protective cover 28.
The utility model reduces trafficking step, by mixing atomization moisture, water tank in batch mixing by being molded immediately after batch mixing The interior moisture for adding the ratio calculated, mixing roller is interior to add the quality for calculating ultrafine powder, open check valve, by fixation After the moisture of amount is fully atomized, the water after atomization is mixed with ultra micro powder, discharges after abundant batch mixing stirring, adds immediately after discharging Enter in comminutor housing, rolled by driving the synergy of pelletizing drum and driven pelletizing drum, and by driving, driven be granulated Granulation groove on cylinder, by the particle made by tilt blanking plate to discharging sieve plate transport, until by meet slot size into Type particle sifts out, and completes whole granulation process.
Above example is the exemplary illustration to this patent, does not limit its protection domain, people in the art Member can also be changed to its part, as long as no the Spirit Essence beyond this patent, all in the protection domain of this patent.

Claims (5)

1. a kind of ultrafine powder Squeezinggranulator, it is characterised in that including frame (1), drive device (2), motor rack (3), mixed Bin (4), frame (5), mixing device (6), prilling granulator (7) are granulated, motor rack (3) is respectively arranged with the frame (1), is mixed Bin (4) and frame (5) is granulated, drive device (2), the drive device (2) and the batch mixing are provided with the motor rack (3) Device (6) is connected, and the mixing device (6) is connected by shaft coupling (8) with prilling granulator (7), described prilling granulator (7) one end Discharging sieve plate (9) is provided with, multigroup sieve aperture (10) is provided with the discharging sieve plate (9);
The drive device (2) includes motor (11), and the motor (11) is fixedly mounted on the motor rack (3) On, motor (11) main shaft is fixedly connected with the driving pulley (12), and the driving pulley (12) is by being driven skin Band is connected with driven pulley (13), and the driven pulley (13) is fixedly connected by connecting shaft with the mixing device (6);
The mixing device (6) includes mixing roller (14), and the mixing roller (14) is fixedly mounted on the batch mixing frame (4) On, batch mixing main shaft (15), described batch mixing main shaft (15) one end and the driven pulley are provided with the mixing roller (14) (13) it is fixedly connected, batch mixing main shaft (15) other end is connected by shaft coupling (8) with the prilling granulator (7), described mixed Batch mixing flabellum (16) is additionally provided with material main shaft (15), water atomization plant is additionally provided with the mixing roller (14);
The prilling granulator (7) includes comminutor housing, and the comminutor housing is fixedly mounted on the granulation frame (5), institute State and driving pelletizing drum (17) and driven pelletizing drum (18) are provided with comminutor housing, the driving pelletizing drum (17) is main Axle is fixedly connected by shaft coupling (8) with the batch mixing main shaft (15), and the driving pelletizing drum (17), driven be granulated are rolled Multigroup granulation groove (19) is machined with cylinder (18) respectively, inclination blanking plate, the blanking plate are provided with the comminutor housing Lower is connected in the discharging sieve plate (9), and the discharging sieve plate (9) is fixedly mounted in the frame (1), the comminutor Charge door (29) is provided with housing.
2. a kind of ultrafine powder Squeezinggranulator according to claim 1, it is characterised in that on the mixing roller (14) Charging aperture (20), discharging opening (21) and atomization mouth (22), the discharging opening (21) are machined with respectively is arranged on the mixing roller (14) bottom, the atomization mouth (22) are provided with the water atomization plant.
3. a kind of ultrafine powder Squeezinggranulator according to claim 2, it is characterised in that the water atomization plant includes Housing (23) is atomized, atomization water tank (24) is provided with the atomization housing (23), the atomization water tank (24) passes through downcomer Road (25) is connected with the atomization housing (23), and ultrasonic atomization piece (26) is set in the atomization housing (23).
4. a kind of ultrafine powder Squeezinggranulator according to claim 3, it is characterised in that set on the drainage pipeline There is check valve (27).
A kind of 5. ultrafine powder Squeezinggranulator according to claim 1, it is characterised in that the driving pulley (12), Driven pulley (13) outer end is respectively arranged with belt wheel protective cover (28).
CN201720314271.3U 2017-03-29 2017-03-29 A kind of ultrafine powder Squeezinggranulator Expired - Fee Related CN206853625U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720314271.3U CN206853625U (en) 2017-03-29 2017-03-29 A kind of ultrafine powder Squeezinggranulator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720314271.3U CN206853625U (en) 2017-03-29 2017-03-29 A kind of ultrafine powder Squeezinggranulator

Publications (1)

Publication Number Publication Date
CN206853625U true CN206853625U (en) 2018-01-09

Family

ID=60815900

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720314271.3U Expired - Fee Related CN206853625U (en) 2017-03-29 2017-03-29 A kind of ultrafine powder Squeezinggranulator

Country Status (1)

Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113102213A (en) * 2021-03-11 2021-07-13 青岛新理工智赢环境管理有限公司 Micro-battery spontaneous sewage treatment agent processing equipment and preparation method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113102213A (en) * 2021-03-11 2021-07-13 青岛新理工智赢环境管理有限公司 Micro-battery spontaneous sewage treatment agent processing equipment and preparation method thereof

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GR01 Patent grant
GR01 Patent grant
CP01 Change in the name or title of a patent holder

Address after: 528000 Shang Jin Ou Development Zone, Xiqiao Town, Nanhai District, Foshan, Guangdong

Patentee after: Guangdong dixingwei Industrial Co.,Ltd.

Patentee after: FOSHAN University

Address before: 528000 Shang Jin Ou Development Zone, Xiqiao Town, Nanhai District, Foshan, Guangdong

Patentee before: FOSHAN DIXINGWEI AUTOMATION EQUIPMENT Co.,Ltd.

Patentee before: FOSHAN University

CP01 Change in the name or title of a patent holder
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180109

CF01 Termination of patent right due to non-payment of annual fee