CN207134435U - A kind of high-efficiency battery raw material spray dryer - Google Patents

A kind of high-efficiency battery raw material spray dryer Download PDF

Info

Publication number
CN207134435U
CN207134435U CN201721195047.3U CN201721195047U CN207134435U CN 207134435 U CN207134435 U CN 207134435U CN 201721195047 U CN201721195047 U CN 201721195047U CN 207134435 U CN207134435 U CN 207134435U
Authority
CN
China
Prior art keywords
high speed
raw material
granulation chamber
speed centrifugal
battery raw
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
CN201721195047.3U
Other languages
Chinese (zh)
Inventor
邵忠宝
周强
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.)
Chongqing Sayadi Lithium Battery Energy Polytron Technologies Inc
Original Assignee
Chongqing Sayadi Lithium Battery Energy Polytron Technologies Inc
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 Chongqing Sayadi Lithium Battery Energy Polytron Technologies Inc filed Critical Chongqing Sayadi Lithium Battery Energy Polytron Technologies Inc
Priority to CN201721195047.3U priority Critical patent/CN207134435U/en
Application granted granted Critical
Publication of CN207134435U publication Critical patent/CN207134435U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Abstract

The utility model discloses a kind of high-efficiency battery raw material spray dryer,Including body,The outside middle position of the body is welded and fixed organic frame,The side of the frame is provided with electric cabinet,The inside of the electric cabinet is provided with AT89S52 controllers,And inlayed on the preceding table wall of electric cabinet and be provided with control panel,The bottom of the body is provided with air blower,And being internally provided with for body dries granulation chamber,Electric heating block is installed in the interlayer that the body is formed with drying granulation chamber,The lower section side of the body is connected with discharger by discharge pipe,The top of the utility model body is hollow cylindrical structure,The bottom of body is open circles bench-type structure,By air blower operation duration constantly to drying granulation chamber inside be pumped into air,And form whirlwind in the bottom of drying granulation chamber,Whirlwind blow cocurrent from the bottom to top and under hot-air and battery stoste,The two is set fully to contact,Drying is finished product within the extremely short time.

Description

A kind of high-efficiency battery raw material spray dryer
Technical field
The utility model belongs to battery processing technique field, and in particular to a kind of high-efficiency battery raw material spray dryer.
Background technology
Spray dryer is a kind of device that can complete to dry and be granulated simultaneously, and feed pump can be adjusted by technological requirement Pressure, flow, the size of spray orifice, obtain the required spheric granules that ratio is sized, spray dryer is continous way One kind of atmospheric dryer, with special installation by liquid material atomisation, it is set to be dried with hot air.Have for drying Liquid, suspension and the viscous liquid of a little thermal sensitivity, are also used for drying fuel, intermediate, soap powder and inorganic salts etc., general bag Include electric drying oven with forced convection, vacuum drying chamber, Highspeedcentrifugingandsprayingdrier, sterile spray dryer.
But battery raw material spray dryer in the market is not only complicated, and function is single, hot-air with Battery stoste can not be contacted fully, and percentage of batteries stoste easily falls into the bottom of drying granulation chamber in the presence of self gravitation Accumulation, causes the wasting of resources, and can not fully dry, and need to carry out secondary drying to the finished product of humidity.
Utility model content
The purpose of this utility model is to provide a kind of high-efficiency battery raw material spray dryer, to solve above-mentioned background technology The hot-air of middle proposition can not be contacted fully with battery stoste, and percentage of batteries stoste is easily fallen into the presence of self gravitation The bottom accumulation of granulation chamber is dried, causes the wasting of resources, and can not fully be dried, secondary drying need to be carried out to the finished product of humidity The problem of.
To achieve the above object, the utility model provides following technical scheme:A kind of high-efficiency battery raw material spray dryer, Including body, the outside middle position of the body is welded and fixed organic frame, and the side of the frame is provided with electric cabinet, institute The inside for stating electric cabinet is provided with AT89S52 controllers, and is inlayed on the preceding table wall of electric cabinet and be provided with control panel, the machine The bottom of body is provided with air blower, and being internally provided with for body dries granulation chamber, and the body is formed with drying granulation chamber Electric heating block is installed in interlayer, the lower section side of the body is connected with discharger by discharge pipe, the discharger it is outer Portion's middle position is welded with discharger support, and the bottom of discharger is provided with Blowing stopper, the inside of the Blowing stopper Impeller is provided with, vapours input channel is installed, and high speed centrifugation is installed at the top of body at the upper side of the body Atomizer housing, one end that the high speed centrifugal atomization device housing is extended to inside drying granulation chamber are provided with high speed centrifugation atomization Device rotating disk, high speed centrifugal atomization device motor and battery raw material input pipe are installed above the high speed centrifugal atomization device housing Road, the battery raw material input channel be arranged on high speed centrifugal atomization device motor side, the high speed centrifugal atomization device motor, Electric heating block, air blower and Blowing stopper are electrically connected with AT89S52 controllers, the AT89S52 controllers and control panel electricity Property connection.
Preferably, the high speed centrifugal atomization device motor is connected with high speed centrifugal atomization device rotating disk by axis of rotation.
Preferably, the body includes upper and lower part, and the top of the body is hollow cylindrical structure, the body Bottom be open circles bench-type structure.
Preferably, one end of the air blower and the bottom of body are connected by pipeline, and the other end passes through bolt with frame It is fixedly connected.
Preferably, the electric heating block is provided with eight altogether, and eight electric heating blocks are bolted on the inwall of body On.
The utility model compared with prior art, has the advantages that:
(1) the utility model body includes upper and lower part, and the top of body is hollow cylindrical structure, the bottom of body For open circles bench-type structure, by air blower operation duration constantly to being pumped into air inside drying granulation chamber, and drying Whirlwind is formed in the bottom of granulation chamber, whirlwind blows cocurrent and lower hot-air and battery stoste, makes the two abundant from the bottom to top Contact, drying is finished product within the extremely short time.
(2) the utility model electric heating block is provided with eight altogether, and eight electric heating blocks are bolted on the interior of body On wall, drying granulation chamber is internally heated by electric heating block work, granular battery raw material will be formed and fully dried.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model;
Fig. 2 is outside drawing of the present utility model;
Fig. 3 is a-quadrant mplifying structure schematic diagram of the present utility model;
In figure:1- high speed centrifugal atomization devices rotating disk, 2- battery raw materials input channel, 3- high speed centrifugal atomization devices motor, 4- High speed centrifugal atomization device housing, 5- vapours input channel, 6- drying granulation chamber, 7- electric cabinets, 8- frames, 9- air blowers, 10- Discharger support, 11- dischargers, 12- electric heating blocks, 13- bodies, 14- discharge pipes, 15- Blowing stoppers, 16- impellers, 17- AT89S52 controllers, 18- control panels.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made The every other embodiment obtained, belong to the scope of the utility model protection.
Fig. 1-3 are referred to, the utility model provides a kind of technical scheme:A kind of high-efficiency battery raw material spray dryer, bag Body 13 is included, the outside middle position of body 13 is welded and fixed organic frame 8, and granulation chamber 6 is dried to support, and the one of frame 8 Side is provided with electric cabinet 7, and the inside of electric cabinet 7 is provided with AT89S52 controllers 17, is started by AT89S52 controllers 17, controlled High speed centrifugal atomization device motor 3, electric heating block 12, air blower 9 and Blowing stopper 15 processed work, and are inlayed on the preceding table wall of electric cabinet 7 Control panel 18 is provided with, the bottom of body 13 is provided with air blower 9, and being internally provided with for body 13 dries granulation chamber 6, uses So that processing is dried, be granulated to battery stoste, electric heating block 12 is installed in the interlayer that body 13 is formed with drying granulation chamber 6, The lower section side of body 13 is connected with discharger 11 by discharge pipe 14, and the outside middle position of discharger 11 is welded and fixed There is discharger support 10, and the bottom of discharger 11 is provided with Blowing stopper 15, Blowing stopper 15 is internally provided with impeller 16, passed through The work of Blowing stopper 15 impeller 16 rotates, and is discharged, and the upper side of body 13 is provided with vapours input channel 5, and The top of body 13 is provided with high speed centrifugal atomization device housing 4, and high speed centrifugal atomization device housing 4 is extended in drying granulation chamber 6 The one end in portion is provided with high speed centrifugal atomization device rotating disk 1, and the top of high speed centrifugal atomization device housing 4 is provided with high speed centrifugation atomization Device motor 3 and battery raw material input channel 2, battery raw material input channel 2 are arranged on the side of high speed centrifugal atomization device motor 3, High speed centrifugal atomization device motor 3, electric heating block 12, air blower 9 and Blowing stopper 15 are electrically connected with AT89S52 controllers 17, AT89S52 controllers 17 are electrically connected with control panel 18.
In the present embodiment, it is preferred that high speed centrifugal atomization device motor 3 is turned with high speed centrifugal atomization device rotating disk 1 by rotating shaft Dynamic connection, is worked by high speed centrifugal atomization device motor 3 and drives high speed centrifugal atomization device rotating disk 1 to rotate at a high speed so that battery is former Liquid rotation at a high speed in high speed centrifugal atomization device housing 4, form imperceptible vaporific liquid pearl and enter in drying granulation chamber 6 and by heat The hot-air current contacting inputted at steam input pipe road 5, form finished product.
In the present embodiment, it is preferred that body 13 includes upper and lower part, and the top of body 13 is hollow cylindrical structure, The bottom of body 13 is open circles bench-type structure, constantly empty to suction inside drying granulation chamber 6 by the operation duration of air blower 9 Gas, and form whirlwind in the bottom of drying granulation chamber 6, whirlwind blow cocurrent and lower hot-air and battery original from the bottom to top Liquid, the two is set fully to contact, drying is finished product within the extremely short time.
In the present embodiment, it is preferred that one end of air blower 9 is connected with the bottom of body 13 by pipeline, the other end and machine Frame 8 is bolted to connection, and is worked by air blower 9 and is dried air continual be pumped into inside granulation chamber 6.
In the present embodiment, it is preferred that electric heating block 12 is provided with eight altogether, and eight electric heating blocks 12 are bolted on On the inwall of body 13, worked by electric heating block 12 and drying granulation chamber 6 is internally heated, it is former that granular battery will be formed Material fully drying.
Operation principle and process for using of the present utility model:Carrying out in use, vapours input channel 5 is added with air Thermal is connected, and battery raw material input channel 2 is connected with battery raw material mother liquor tank, the utility model is connected with power supply, In the presence of blower fan, the air by air heating means heats, filtration treatment is uniform in the shape of a spiral by vapours input channel 5 Enter drying granulation chamber 6 in, in the presence of single-screw (single screw) pump, in mother liquor tank dissolving, stirring and processing into liquid condition electricity Pond raw material is entered in high speed centrifugal atomization device housing 4 by battery raw material input channel 2, passes through high speed centrifugal atomization device motor 3 Work drives high speed centrifugal atomization device rotating disk 1 to rotate at a high speed, and battery stoste rotates at a high speed in high speed centrifugal atomization device housing 4, Imperceptible vaporific liquid pearl is formed to connect with the hot-air cocurrent inputted by vapours input channel 5 into drying granulation chamber 6 is interior Touch, by the operation duration of air blower 9 constantly to being pumped into air inside drying granulation chamber 6, and in the bottom of drying granulation chamber 6 Interior formation whirlwind, whirlwind blow cocurrent from the bottom to top and under hot-air and battery stoste, extend the two in drying granulation chamber 6 Flotation time so that the two is fully contacted, and worked by electric heating block 12 and drying granulation chamber 6 be internally heated, from And make the drying within the extremely short time of battery stoste be finished product, by Blowing stopper 15 work impeller 16 rotate, by finished product by Extracted out at discharge pipe 14, complete processing.
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art, It is appreciated that these embodiments can be carried out with a variety of changes in the case where not departing from principle of the present utility model and spirit, repaiied Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.

Claims (5)

1. a kind of high-efficiency battery raw material spray dryer, including body(13), it is characterised in that:The body(13)Outside in Between opening position be welded and fixed organic frame(8), the frame(8)Side be provided with electric cabinet(7), the electric cabinet(7)It is interior Portion is provided with AT89S52 controllers(17), and electric cabinet(7)Preceding table wall on inlay and be provided with control panel(18), the machine Body(13)Bottom air blower is installed(9), and body(13)Be internally provided with drying granulation chamber(6), the body(13) With drying granulation chamber(6)Electric heating block is installed in the interlayer of formation(12), the body(13)Lower section side pass through discharge nozzle Road(14)It is connected with discharger(11), the discharger(11)Outside middle position be welded with discharger support (10), and discharger(11)Bottom Blowing stopper is installed(15), the Blowing stopper(15)Be internally provided with impeller(16), institute State body(13)Upper side vapours input channel is installed(5), and body(13)Top high speed centrifugation mist is installed Change device housing(4), the high speed centrifugal atomization device housing(4)Extend to drying granulation chamber(6)Internal one end is provided with a high speed Centrifugal atomizer rotating disk(1), the high speed centrifugal atomization device housing(4)Top high speed centrifugal atomization device motor is installed(3) With battery raw material input channel(2), the battery raw material input channel(2)Installed in high speed centrifugal atomization device motor(3)One Side, the high speed centrifugal atomization device motor(3), electric heating block(12), air blower(9)And Blowing stopper(15)Controlled with AT89S52 Device(17)It is electrically connected with, the AT89S52 controllers(17)With control panel(18)It is electrically connected with.
A kind of 2. high-efficiency battery raw material spray dryer according to claim 1, it is characterised in that:The high speed centrifugation mist Change device motor(3)With high speed centrifugal atomization device rotating disk(1)Connected by axis of rotation.
A kind of 3. high-efficiency battery raw material spray dryer according to claim 1, it is characterised in that:The body(13)Bag Include upper and lower part, the body(13)Top be hollow cylindrical structure, the body(13)Bottom be hollow round table Type structure.
A kind of 4. high-efficiency battery raw material spray dryer according to claim 1, it is characterised in that:The air blower(9) One end and body(13)Bottom connected by pipeline, the other end and frame(8)It is bolted to connection.
A kind of 5. high-efficiency battery raw material spray dryer according to claim 1, it is characterised in that:The electric heating block(12) Eight, and eight electric heating blocks are provided with altogether(12)It is bolted on body(13)Inwall on.
CN201721195047.3U 2017-09-18 2017-09-18 A kind of high-efficiency battery raw material spray dryer Expired - Fee Related CN207134435U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721195047.3U CN207134435U (en) 2017-09-18 2017-09-18 A kind of high-efficiency battery raw material spray dryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721195047.3U CN207134435U (en) 2017-09-18 2017-09-18 A kind of high-efficiency battery raw material spray dryer

Publications (1)

Publication Number Publication Date
CN207134435U true CN207134435U (en) 2018-03-23

Family

ID=61638649

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721195047.3U Expired - Fee Related CN207134435U (en) 2017-09-18 2017-09-18 A kind of high-efficiency battery raw material spray dryer

Country Status (1)

Country Link
CN (1) CN207134435U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI670108B (en) * 2018-06-12 2019-09-01 豐能科技股份有限公司 Dry sprayer structure

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI670108B (en) * 2018-06-12 2019-09-01 豐能科技股份有限公司 Dry sprayer structure

Similar Documents

Publication Publication Date Title
CN204313610U (en) A kind of raw material processing Drying
CN205073968U (en) Fluid bed granulator
CN103604281A (en) Rotary drum dryer
CN207134435U (en) A kind of high-efficiency battery raw material spray dryer
CN209128299U (en) A kind of garbage sludge anhydration system
CN208346022U (en) A kind of stagewise sludge drier
CN203663470U (en) Traditional Chinese medicine spray dryer
CN208635432U (en) A kind of polyaluminium chloride drying device
CN206315486U (en) A kind of spray drying device
CN203132306U (en) Automatic smashing drying machine
CN205965060U (en) High -speed centrifugal spray drying equipment suitable for preparation dibazolum capsule
CN205516556U (en) A high -speed centrifugal spray drier for blueberry leaf draws
CN202186954U (en) Spray drying device
CN203899176U (en) Rotating spray drying system
CN207871566U (en) A kind of centrifugal spray drying device
CN207126149U (en) Spray drier for Chinese medicine extract
CN100351313C (en) Vacuum drying method of carbon dioxide full base degradation plastic-polypropylidene carbonate and its device
CN107441747A (en) A kind of vacuum spray dehydrator group and method
CN103752025A (en) Spray dryer
CN203908228U (en) Particle drying device
CN203648107U (en) Spray dryer
CN104556028B (en) Method for realizing rapid, sealed and continuous production of super-bamboo activated carbon and clean production assembly line thereof
CN205482107U (en) Stick with paste drying system with polyvinyl chloride reclaimed materials
CN209302204U (en) Drying machine with centrifugal spray
CN204648833U (en) A kind of spray tower, fluid bed Combined drying equipment

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180323

Termination date: 20180918