CN2905177Y - Ferrite slurry conveying appliance - Google Patents
Ferrite slurry conveying appliance Download PDFInfo
- Publication number
- CN2905177Y CN2905177Y CN 200620103952 CN200620103952U CN2905177Y CN 2905177 Y CN2905177 Y CN 2905177Y CN 200620103952 CN200620103952 CN 200620103952 CN 200620103952 U CN200620103952 U CN 200620103952U CN 2905177 Y CN2905177 Y CN 2905177Y
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- tower body
- pipeline
- conveying device
- storage vat
- conveyance conduit
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Abstract
The utility model relates to a conveying device for ferrite pulp, combining auto dehydrating and auto seal and conveying for ferrite magnet, realizing conformity and continuous supply for pulp water content; the device comprises a discharge device (6), a convey pipeline (3) and a storage tank (4) which divides current. The utility model is characterized in that the discharge device (6) is provided with a auto dehydrating device (1), comprising a tower body (13), a power transmission device which is arranged at the top of the auto dehydrating device (1), a mixing device inside the auto dehydrating device (1) and a drain control device at the outer side of the auto dehydrating device (1). The power transmission device and the mixing device are arranged on the main shaft (15) from top to bottom of the tower.
Description
Technical field
The utility model relates to the technical field of a kind of employed automatic dehydration of permanent-magnet ferrite magnetic material industry and pipe conveying equipment, is a kind of conveying device of ferrite slurry specifically.
Background technology
The production of permanent-magnet ferrite magnetic material need be carried out wet ball grinding, could obtain good magnetic property like this.(50~60wt%) (wt% refers to percentage by weight), can not be directly used in moulding production, the water content of slip need be sloughed a part, just is fit to moulding when requiring water content to reach 30~40wt% and uses and the slip water content of wet ball grinding is too high.The at present domestic method that on the slurry dewatering operation, all adopts natural sedimentation dehydration (as with precipitating ground, precipitator tower and drainage frame etc.), a dead lift (as charging basket, truck etc.).Exist that the slip pipeline is carried non-automaticization, dehydration back slip water content is inconsistent, the production cycle long, environment is poor, labour intensity is big, be unfavorable for problem such as automatic injection forming with these methods, influence consistency of product and stability.
As mentioned above, there is following deficiency in prior art: the slip pipeline is carried non-automaticization, the slip water content is inconsistent, the production cycle long, environment is poor, labour intensity is big, be unfavorable for automatic injection forming, and consistency of product and stable bad.
Summary of the invention
The utility model has solved that the slip pipeline that prior art exists is carried non-automaticization, the slip water content is inconsistent, the production cycle long, environment is poor, labour intensity is big, be unfavorable for automatic injection forming, and consistency of product and the bad problem of stability, provide a kind of automation sealing to carry slip, and the pipeline transporter of the ferrite slurry that environmental pollution is low, production efficiency is high and labour intensity is low, it has realized the automatic dehydration of permanent ferrite slurry, makes the uniformity of slip water content supply with continuous.
Above-mentioned technical purpose of the present utility model mainly solves by the following technical programs: a kind of conveying device of ferrite slurry, comprise drawing mechanism, conveyance conduit and with the storage vat of its shunting, it is characterized in that described drawing mechanism is provided with the automatic dehydration device, it comprises tower body, be located at the power transmission at tower body top, be located at the agitating device of tower body inside and be located at the drain control unit in the tower body outside, and described power transmission and described agitating device are located on the main shaft at the bottom of from cat head to tower in proper order.The utility model comprises that automatic dehydration and pipeline carry two processes of slip, and what the automatic dehydration process adopted is that centrifugal sedimentation and gravitational settling combine, and adds principle design that screw extrusion advances; The tower body of design is circular, has so just strengthened the speed of gravitational settling and centrifugal sedimentation; And helical blade and the planetary reduction gear connection that is arranged on the tower body top are equipped with for stirring vane, lower end in middle main shaft upper end, have the double effects that stirs and advance slip; The tower body upper inner is designed to sandwich, on the internal layer side, be provided with equally distributed aperture, and, so just can realize draining voluntarily in the above by last filter cloth, and the slip particle can not flow out yet, and drain control unit can be according to the switch of how many automatic pressure regulation valves of the water yield; And pipeline is carried in the slip process, after the dehydration of slip, enter into pipeline by discharging opening through the automatic dehydration device, in the discharge tank that a part is diverted to pipeline is connected, another part just is back in the tower body by pipeline, is particularly suitable for 24 continuous throughout the twenty-four hour24s then.Solved the problem that slip is carried in permanent ferrite slurry automation dehydration and automation like this, satisfied the demand of producing, the uniformity of slip water content and supply have continuously been realized, reduced environmental pollution and alleviated labour intensity, made it improve production efficiency and consistency of product and stability.
As preferably, described tower body inside upper part is provided with uniform foraminate interlayer, interlayer one side that is provided with aperture is provided with filter cloth, such design, can not only make water from interlayer, discharge voluntarily the equally distributed aperture, and a side that is provided with aperture at interlayer by on filter cloth, can make the slip particle can from aperture, not flow out; Described tower body lower inside is provided with material chamber, bottom, described material chamber is connected with discharging opening, described discharging opening connects conveyance conduit one end by delivery pump, the described conveyance conduit other end connects the tower body top and tower body communicates, utilize delivery pump that slip is transported in the pipeline, because slip has concentration height, free settling, delivery pump selects for use pressure to reach plunger displacement pump, membrane pump or the screw pump of 5MPa.
As preferably, described conveyance conduit connects some storage vats by some parallel tube connectors, and described tube connector pipeline is provided with magnetic valve; Described conveyance conduit is back-shaped pipeline.This conveyance conduit is selected seamless steel pipe or gapless stainless steel tube for use, its diameter is not less than 50mm, and the bigger elbow of radius of turn is selected at the turning for use, the elbow radius greater than 100mm to reduce resistance, and pipeline path is designed to back-shaped structure with anti-clogging, and helps flushing pipe; This tube connector is the charging mouth of pipe of storage vat, and storage vat is used for storing the slip that conveyance conduit flows into, and whether enters storage vat and magnetic valve is used for controlling slip exactly.
As preferably, described power transmission comprises drive motors and planetary reduction gear, described planetary reduction gear one end links to each other with drive motors, the other end is connected with the tower body top, open drive motors, through the transmission of planetary reduction gear, reduce rotating speed, make rotating speed be fit to the needs of automatic dehydration device mixing speed; Described agitating device comprises the several layers stirring vane and is positioned at the helical blade of its lower end, helical blade has certain helical angle, when stirring vane and helical blade under the driving at drive motors with certain rotary speed working, rotation direction when stirring vane and helical blade rotation is downward, thereby produce downward thrust when rotating, make slip to material chamber bottom squeeze, because the double action of gravity of slip own and extruding force, slip can reach certain concentration in the material chamber, bottom, if the height of adaptive adjustment tower body and diameter ratio, the helical angle of helical blade, and the rotating speed of main shaft can be stablized the slip that obtains certain adjustable water content; Described drain control unit comprises the pressure valve of an end in pipeline and setting and the pipeline, the described pipeline other end and interlayer communicate, when the slip of material chamber, bottom reaches finite concentration, the moisture on tower body top sees through filter cloth and enters in the interlayer, flow to again with pipeline that interlayer is connected in, and after water enters into pipeline, be installed in ducted pressure valve and just can have so just realized the automatic dehydration to slip according to how many control drainings automatically of the water yield.
As preferably, be provided with the power transmission that comprises position sensor, is located at the storage vat top, the stirring vane of being located at storage vat inside in the described storage vat, described power transmission and stirring vane are located on the main shaft at the bottom of storage vat pushes up storage vat in proper order.This position sensor is to be used for the magnetic valve that the control connection pipeline is provided with, and to realize the automatic control reinforced to each storage vat, the stirring vane that is provided with in the storage vat is in order to keep the uniformity of slip water content.
As preferably, the height of described tower body and diameter ratio are 1/5~1/2; The spiral angle of described helical blade is 10~20 °.Through the helical angle of the height of adjusting tower body and diameter ratio, helical blade, and the rotating speed of main shaft, can stablize the slip that obtains desired moisture content.
As preferably, the diameter of described tube connector is 1/4~3/4 of a pipe diameter.With the tube connector diameter is half the best of pipe diameter, keeps that so certain pressure is arranged in the conveyance conduit, is beneficial to slip and flows into storage vat.
The utility model is skillfully constructed, carry with the automatic dehydration of permanent ferrite slurry with from movable sealing to combine, realized the uniformity of slip water content and supply with continuously, reduced environmental pollution, alleviated labour intensity, improved production efficiency and consistency of product and stability, reduced production cost.
Description of drawings
Fig. 1 is a kind of structural representation of the present utility model:
Fig. 2 is the structural representation of the utility model automatic dehydration device.
The specific embodiment
Below by embodiment, and in conjunction with the accompanying drawings, the technical solution of the utility model is described further.
Embodiment 1.See Fig. 1 and Fig. 2, the conveying device of this routine a kind of ferrite slurry, comprise drawing mechanism 6, conveyance conduit 3 and with the storage vat 4 of its shunting, described drawing mechanism 6 is provided with automatic dehydration device 1, the drain control unit that it comprises tower body 13, is located at the power transmission at tower body 13 tops, is located at the agitating device of tower body 13 inside and is located at tower body 13 outsides, described power transmission and described agitating device are located on the main shaft 15 at the bottom of from cat head to tower in proper order; Described tower body 13 inside upper part are provided with uniform foraminate interlayer 22, interlayer 22 1 sides that are provided with aperture are provided with filter cloth 18, described tower body 13 lower inside are provided with material chamber 14, bottom, described material chamber 14 is connected with discharging opening 19, described discharging opening 19 connects conveyance conduit 3 one ends by delivery pump 2, and described conveyance conduit 3 other ends connect tower body 13 tops and tower body communicates; Described conveyance conduit 3 is back-shaped pipeline, and it connects some storage vats 4 by some parallel tube connectors 7, and described tube connector 7 pipelines are provided with magnetic valve 8, and the diameter of tube connector 7 is that the diameter of storage vat charging aperture is 1/2 of conveyance conduit 3 diameters; Described power transmission comprises drive motors 11 and planetary reduction gear 12, and described planetary reduction gear 12 1 ends link to each other with drive motors 11, and the other end is connected with tower body 13 tops; Described agitating device comprises several layers stirring vane 16 and is positioned at the helical blade 17 of its lower end; Described drain control unit comprises the pressure valve 21 of an end in pipeline 20 and setting and the pipeline 20, and described pipeline 20 other ends and interlayer 22 communicate; Be provided with the power transmission that comprises position sensor, is located at the storage vat top, the stirring vane of being located at storage vat inside in the described storage vat 4, described power transmission and stirring vane are located on the main shaft at the bottom of storage vat pushes up storage vat in proper order; The height of described tower body 13 and diameter ratio are 1/3; The spiral angle of described helical blade 17 is 15 °.
During work, after the ball milling slip is sent into tower body 13 by delivery pump, opening drive motors 11 drive main shafts 15 rotates with rotating speed 5~15r/min, and drive is provided with thereon stirring vane 16 and helical blade 17 work, because the direction of rotation of stirring vane 16 and helical blade 17 is downward, produce downward thrust during rotation, make slip to material chamber bottom squeeze; Because the double action of gravity of slip own and extruding force, slip can reach certain concentration in the material chamber, bottom; The moisture on tower body 13 tops can see through the filter cloth 18 that is pasting on the interlayer 22 and enter in the interlayer 22, flow to again in the pipeline 20 that is connected with interlayer 22, and after water enters into pipeline 20, the pressure valve 21 that is installed in the pipeline 20 just can according to how many control drainings automatically of the water yield, promptly, the water yield regularly opens the valve draining automatically when reaching one, and automatic-closing valve when being lower than certain position prevents that moisture is low excessively, has so just realized the automatic dehydration to slip; During discharging, the discharging opening 19 that turn on agitator and material chamber, bottom 14 are provided with, because the thrust that the helical blade rotation produces, slip just can flow out from discharging opening 19 smoothly; When height and the diameter ratio of adjusting tower body are between 1/5~1/2, the helical angle of helical blade is between 10~20 °, and the rotating speed of main shaft be between 5~15r/min the time, can stablize with this understanding and obtain the slip that desired moisture content is 30~40% (adjustable), and can move continuously.
After slip just flows out from discharging opening 19, by delivery pump 2 slip is transported in the conveyance conduit 3, when slip flows into wherein through tube connector 7 part branches, be arranged in the storage vat 4 position sensor just control be arranged on the unlatching of each way solenoid valve 8 in the tube connector 7 or close, to realize the auto feed of storage vat, and another part just flows back to tower body 13 along conveyance conduit, and can flushing pipe; The electric control system that electrical equipment such as automatic dehydration device 1, delivery pump 2, each way solenoid valve 8, pressure valve 21 and position sensor are formed is installed concentratedly in electric appliance control box 5.
Qualified slip is come out by material chamber bottom discharge mouth through dewatering, send into conveyance conduit 3 through delivery pump 2, slip is transported in the other storage vat 4 of assembly room mo(u)ldenpress, realizes the automatic dehydration and the sealing of slip are carried, be particularly suitable for 24 continuous throughout the twenty-four hour24s.
Claims (8)
1, a kind of conveying device of ferrite slurry, comprise drawing mechanism (6), conveyance conduit (3) and with the storage vat (4) of its shunting, it is characterized in that described drawing mechanism (6) is provided with automatic dehydration device (1), it comprises tower body (13), be located at the power transmission at tower body (13) top, be located at the inner agitating device of tower body (13) and be located at the drain control unit in tower body (13) outside, and described power transmission and described agitating device are located on the main shaft (15) at the bottom of from cat head to tower in proper order.
2, the conveying device of ferrite slurry according to claim 1, it is characterized in that described tower body (13) inside upper part is provided with uniform foraminate interlayer (22), interlayer (22) one sides that are provided with aperture are provided with filter cloth (18), described tower body (13) lower inside is provided with material chamber (14), bottom, described material chamber (14) is connected with discharging opening (19), described discharging opening (19) connects conveyance conduit (3) one ends by delivery pump (2), and described conveyance conduit (3) other end connects tower body (13) top and tower body communicates.
3, the conveying device of ferrite slurry according to claim 1 and 2 is characterized in that described conveyance conduit (3) connects some storage vats (4) by some parallel tube connectors (7), and described tube connector (7) pipeline is provided with magnetic valve (8).
4, the conveying device of ferrite slurry according to claim 1, it is characterized in that described power transmission comprises drive motors (11) and planetary reduction gear (12), described planetary reduction gear (12) one ends link to each other with drive motors (11), and the other end is connected with tower body (13) top; Described agitating device comprises several layers stirring vane (16) and is positioned at the helical blade (17) of its lower end; Described drain control unit comprises the pressure valve (21) of an end in pipeline (20) and setting and the pipeline (20), and described pipeline (20) other end and interlayer (22) communicate.
5, the conveying device of ferrite slurry according to claim 3, it is characterized in that being provided with the power transmission that comprises position sensor, is located at the storage vat top, the stirring vane of being located at storage vat inside in the described storage vat (4), described power transmission and stirring vane are located on the main shaft at the bottom of storage vat pushes up storage vat in proper order.
6, the conveying device of ferrite slurry according to claim 3 is characterized in that described conveyance conduit (3) is back-shaped pipeline.
7,, it is characterized in that the height of described tower body (13) and diameter ratio are 1/5~1/2 according to the conveying device of claim 1 or 4 described ferrite slurries; The spiral angle of described helical blade (17) is 10~20 °.
8, the conveying device of ferrite slurry according to claim 3, the diameter that it is characterized in that described tube connector (7) are 1/4~3/4 of conveyance conduit (3) diameter.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200620103952 CN2905177Y (en) | 2006-05-25 | 2006-05-25 | Ferrite slurry conveying appliance |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN 200620103952 CN2905177Y (en) | 2006-05-25 | 2006-05-25 | Ferrite slurry conveying appliance |
Publications (1)
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CN2905177Y true CN2905177Y (en) | 2007-05-30 |
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CN 200620103952 Expired - Fee Related CN2905177Y (en) | 2006-05-25 | 2006-05-25 | Ferrite slurry conveying appliance |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104150223A (en) * | 2014-08-15 | 2014-11-19 | 鞍山市德康磁性材料有限责任公司 | Permanent magnetic ferrite sizing agent remote conveying system |
CN105134611A (en) * | 2015-09-23 | 2015-12-09 | 广州市拓道流体设备技术有限公司 | Residue pulp pump and delivery device thereof |
TWI565950B (en) * | 2014-02-12 | 2017-01-11 | Aoi Seiki Co Ltd | Handling device |
US9776811B2 (en) | 2015-03-31 | 2017-10-03 | Aoi Seiki Co., Ltd. | Conveying device |
-
2006
- 2006-05-25 CN CN 200620103952 patent/CN2905177Y/en not_active Expired - Fee Related
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI565950B (en) * | 2014-02-12 | 2017-01-11 | Aoi Seiki Co Ltd | Handling device |
US9766258B2 (en) | 2014-02-12 | 2017-09-19 | Aoi Seiki Co., Ltd. | Carrying apparatus |
CN104150223A (en) * | 2014-08-15 | 2014-11-19 | 鞍山市德康磁性材料有限责任公司 | Permanent magnetic ferrite sizing agent remote conveying system |
US9776811B2 (en) | 2015-03-31 | 2017-10-03 | Aoi Seiki Co., Ltd. | Conveying device |
CN105134611A (en) * | 2015-09-23 | 2015-12-09 | 广州市拓道流体设备技术有限公司 | Residue pulp pump and delivery device thereof |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Dongyang Fushite Magnetic Industry Co., Ltd. Assignor: Li Lingfeng Contract record no.: 2011330001008 Denomination of utility model: Ferrite slurry conveying appliance Granted publication date: 20070530 License type: Exclusive License Record date: 20110722 |
|
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070530 Termination date: 20140525 |