CN202984174U - Micro powder purification production device - Google Patents

Micro powder purification production device Download PDF

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Publication number
CN202984174U
CN202984174U CN 201220692964 CN201220692964U CN202984174U CN 202984174 U CN202984174 U CN 202984174U CN 201220692964 CN201220692964 CN 201220692964 CN 201220692964 U CN201220692964 U CN 201220692964U CN 202984174 U CN202984174 U CN 202984174U
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CN
China
Prior art keywords
tank body
micro mist
process units
discharging
units according
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 - Lifetime
Application number
CN 201220692964
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Chinese (zh)
Inventor
张云香
李保中
郑丽娜
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.)
Henan Fulaige Ultrahard Material Co ltd
Funik Ultrahard Material Co Ltd
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Henan Funik Ultrahard Material Co Ltd
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Priority to CN 201220692964 priority Critical patent/CN202984174U/en
Application granted granted Critical
Publication of CN202984174U publication Critical patent/CN202984174U/en
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Abstract

The utility model discloses a micro powder purification production device which is characterized in that a stirring device is mounted in a tank body; a feed port and discharge ports are formed in the tank body; and when the micro powder purification production device is in use, an acidification raw micro powder material is heated in the tank body through the feed port, then washing water is added to the tank body through the feed port, and the acid-washed raw micro powder material is stirred by the stirring device and washed fully in the washing water simultaneously, so that a purpose of conducting acid-washing on the raw micro powder material is achieved. Therefore, the problem that the working efficiency of micro powder purification is low due to the fact that pH of micro powder can return to be neutral by a manual washing method after the acid-washing in the prior art is solved.

Description

Micro mist purification process units
Technical field
The utility model relates to micro mist purification production technique field, relates in particular to a kind of micro mist purification process units.
Background technology
at present, the acid of micro mist is rinsed the main method of manual flushing that adopts and is completed, namely after to the powder material pickling, with two, 30 myriagrams draw acid fluid to pour respectively a twenty or thirty noggin (the single glass of 2-3 myriagram that feeds intake draws) into to carry out manual flushing, rinse to the acid-base value reply neutrality of fluid, the micro mist that obtains after fluid drying is dropped on separator carry out sorting, so not only want footprint area large, and in sour flushing process, need constantly to stir with the glue rod, making acid rinse required labour intensity improves greatly, operating efficiency reduces greatly, therefore along with the increase of micro mist output, what material dropped into concentrates, repeatedly control water only according to artificial flushing, not only take manpower, when taking a lot of work, and there are the lot of essential factors such as the wasting of resources in frequent pouring, in case the situation that hysteresis appears in operation is rinsed in acid, the problem that the nothing material can be thrown will appear in automatic fraction collector, thereby affect the purifying velocity of micro mist, extend the production cycle of micro mist processing, increase the production cost that micro mist is purified.
The utility model content
The purpose of this utility model is to provide a kind of micro mist purification process units, is intended to solve in prior art, and micro mist needs by the method that craft is rinsed, acid-base value to be replied after pickling neutral, so that the inefficient problem of micro mist Purification.
In order to realize above purpose, the technical scheme that the utility model adopts is:
Micro mist purification process units, comprise tank body and agitating device, offer on described tank body for the charging aperture that adds powder material and wash water in tank body and for the discharging opening of discharging micro mist product in tank body, described agitating device comprises the stirring vane that is installed in tank body and is used for driving the drive motors that stirring vane rotates, described drive motors is installed in outside tank body, and is in transmission connection with stirring vane.
Described tank body extends along the vertical direction, and tank body has the end cap that is in its top, and described charging aperture and discharging opening all are on described end cap.
The stirring vane of described agitating device is arranged on the tank base position.
Also offer on described end cap for adding the filler of wash water in the light body, and being equiped with the filler pipe of the annular that is communicated with the filler in the side in tank body of end cap, the side in tank body of filler pipe offers at least one group of bleeder that distributes ringwise.
Described discharging opening has at least two, and all is equipped with the discharge nozzle of downward-extension in each discharging opening, and the lower end port of each discharge nozzle all stretches in tank body, and mutually staggers at above-below direction.
Described tank body is outside equipped with the leading truck of downward-extension, on leading truck along the vertical direction guiding be equipped with discharging support, described each discharge nozzle all is fixed on discharging support, and leads along the vertical direction with leading truck by discharging support and coordinate.
Be equiped with the drive unit that moves on leading truck for driving discharging support between described leading truck and discharging support, on drive unit, control connection is useful on the controller of controlling its action.
Be equipped with the evacuated tube for residue after the micro mist product is discharged from tank body, in emptying tank body on described end cap, the lower end of evacuated tube is in the bottom of tank body.
Be equiped with charging hopper on described charge door, the large end of charging hopper is in outside tank body, and the small end of charging hopper stretches in tank body.
Also offer on described tank body for the acid discharge mouth of discharging the acid solution after the flushing water dilution in tank body.
The utility model is equiped with agitating device in tank body, and offer charge door and discharging opening on tank body, in use, add the powder material of acid adding in the tank body by charge door, then add wash water by charge door in tank body, differential raw material by the agitating device stirring and pickling fully rinses in wash water simultaneously, to reach the purpose that acid is rinsed to powder material, thereby solved in prior art, micro mist needs by the method that craft is rinsed, acid-base value to be replied after pickling neutral, so that the low problem of micro mist Purification efficient.
Description of drawings
Fig. 1 is the structural representation of embodiment of the present utility model;
Fig. 2 is the structural representation at end cap inner side place in Fig. 1.
The specific embodiment
The embodiment of micro mist purification process units of the present utility model: as depicted in figs. 1 and 2, this micro mist purification process units comprises tank body 1, agitating device 2, discharging support 3, leading truck 4, drive unit and controller 5, tank body 1 extends along the vertical direction, offers evacuation port, charge door, water inlet 10, discharging opening and the acid discharge mouth that distributes successively from left to right on the end cap of conductor upper end.Be fitted with the lower end in evacuation port and stretch into the evacuated tube 6 of tank body 1 bottom, the lower end port of evacuated tube 6 is in the bottom of tank body 1; Be fitted with charging hopper 7 on charge door, the large end of charging hopper 7 is in outside tank body 1, small end inserts in tank body 1; Be communicated with the filler pipe 11 of the annular of the end cap inboard that is installed in tank body on filler 10, offer a component mouth of a river 12 that distributes ringwise on filler pipe 11; Discharging opening has two pairs and symmetrical centered by agitating device 2 at left and right directions, is fitted with respectively discharge nozzle 8 on each discharging opening, and the lower end port of every pair of discharge nozzle 8 staggers mutually at above-below direction; Be fitted with ACID 9 on the acid discharge mouth, the lower end of ACID 9 is stretched in tank body 1, and the lower end port is in the bottom of tank body 1, and the upper end of ACID 9 is communicated with on the acid discharge water pump.
Each discharge nozzle 8 all is fixed on discharging support 3, discharging support 3 horizontal-extendings, leading truck 4 extends at above-below direction, and material-feeding rack leads along the vertical direction and is assemblied on leading truck 4, be equiped with drive unit between leading truck 4 and discharging support 3, this drive unit be on leading truck 4 installing be in hydraulic trailer between leading truck 4 and discharging support 3, and the drive unit control connection is on controller 5.Agitating device 2 comprises stirring vane and drives the drive motors that stirring vane rotates, and drive motors is in tank body 1 top, and stirring vane is in the base plate position in tank body 1.
the present embodiment in use, add micro mist (cubic boron nitride micro mist) raw material of acid adding in the tank body by charging hopper, inject wash water by the filler in tank body again, and occur to stop up or the water yield wash water of too hour annotating in the tank body by charge door at cleaning hose, by adjusting drive motors, stirring vane is rotated according to predetermined speed simultaneously, so that the fluid in tank body 1 is stirred, until the acid-base value of tank body 1 inner fluid meets the requirements, driving discharge nozzle 8 by discharging support 3 at last moves at above-below direction, make the interior different micro mist of each layer granularity of the corresponding tank body 1 of lower end port of each discharge nozzle 8, and each layer micro mist extracted out by different discharge nozzle 8, carry out the size sorting operation to drop on corresponding separator.
The present embodiment in use, acid flushing and the coarse size sorting of micro mist all realize in the process units of the present embodiment, in the twice production process, material shifts the time that consumes thereby saved, and has improved production efficiency; Make the Fluid Flow in A in tank body 1 in the time of can be by agitating device 2 in the time of acid adding, reach and stir simultaneously and the purpose of acid adding; After pickling is completed, can under the stirring of agitating device 2, the micro mist in fluid fully be cleaned by to a large amount of wash waters of the interior injection of tank body 1, then by discharge gate, the micro mist in tank body 1 be extracted out, reach the purpose that acid is rinsed to powder material.
In the above-described embodiments, offer the acid discharge mouth on the end cap of tank body, to get rid of the acid solution of diluting through wash water in tank body, in other embodiments, also can section offer this acid discharge mouth on tank body, and by discharging opening, the fluid in tank body all be got rid of.
In the above-described embodiments, pneumostome is not set on tank body, thereby be adapted to the less situation of tank body internal gas pressure in process of manufacture, in other embodiments, when the air pressure in tank body is larger in process of manufacture, should offer pneumostome on tank body, so that the eliminating of gas in tank body is avoided because of excessive each sealing station of the tank body that causes of gas pressure in tank body by the hidden danger of spreading.
In the above-described embodiments, be fitted with charging hopper on charge door, to avoid when adding acid solution in tank body, the acid solution potential safety hazard that personal safety to the staff causes of splashing, in other embodiments, also can be by offering acid-adding port on tank body, and plug-in mounting adds acid tube on acid-adding port, the port that stretches in tank body that adds acid tube is inserted below the liquid level of fluid, thereby add acid solution by the acid adding water pump in tank body.
In the above-described embodiments, cooperation by leading truck and discharging support, affect discharge nozzle to move at above-below direction, as much as possible the micro mist in tank body is discharged, in other embodiments, discharge nozzle also can be fixed on tank body, so that the lower end port position of discharge nozzle is fixed, in corresponding tank body, each feeding quantity should be consistent.
In the above-described embodiments, be fitted with a plurality of discharge nozzles on tank body, the lower end port of each discharge nozzle staggers mutually at above-below direction, in other embodiments, also can only offer discharging opening on tank body, and not install discharge nozzle, when discharging, stretch in tank body by flexible pipe, the micro mist in tank body is discharged.
In the above-described embodiments, be equiped with filler pipe on the filler, so that wash water is in filling process, flow from bottom to top in tank body, improve the developing result that acid is rinsed, in other embodiments, also can remove filler and filler pipe, the wash water of directly annotating in the tank body by charge door.
In the above-described embodiments, filler, charge door and discharging opening all are on the end cap of tank body, and in other embodiments, filler, charge door and discharging opening also can be arranged on the sidewall or base plate of tank body.

Claims (10)

1. micro mist purification process units, it is characterized in that, comprise tank body and agitating device, offer on described tank body for the charging aperture that adds powder material and wash water in tank body and for the discharging opening of discharging micro mist product in tank body, described agitating device comprises the stirring vane that is installed in tank body and is used for driving the drive motors that stirring vane rotates, described drive motors is installed in outside tank body, and is in transmission connection with stirring vane.
2. micro mist purification process units according to claim 1, is characterized in that, described tank body extends along the vertical direction, and tank body has the end cap that is in its top, and described charging aperture and discharging opening all are on described end cap.
3. the micro mist according to claim 2 process units of purifying, is characterized in that, the stirring vane of described agitating device is arranged on the tank base position.
4. micro mist purification process units according to claim 2, it is characterized in that, also offer on described end cap for adding the filler of wash water in the light body, and being equiped with the filler pipe of the annular that is communicated with the filler in the side in tank body of end cap, the side in tank body of filler pipe offers at least one group of bleeder that distributes ringwise.
5. micro mist purification process units according to claim 2, it is characterized in that, described discharging opening has at least two, and all is equipped with the discharge nozzle of downward-extension in each discharging opening, the lower end port of each discharge nozzle all stretches in tank body, and mutually staggers at above-below direction.
6. micro mist purification process units according to claim 5, it is characterized in that, described tank body is outside equipped with the leading truck of downward-extension, lead along the vertical direction on leading truck and be equipped with discharging support, described each discharge nozzle all is fixed on discharging support, and leads along the vertical direction with leading truck by discharging support and coordinate.
7. micro mist purification process units according to claim 6, it is characterized in that, be equiped with the drive unit that moves on leading truck for driving discharging support between described leading truck and discharging support, on drive unit, control connection is useful on the controller of controlling its action.
8. micro mist purification process units according to claim 2, is characterized in that, is equipped with the evacuated tube for residue after the micro mist product is discharged from tank body, in emptying tank body on described end cap, and the lower end of evacuated tube is in the bottom of tank body.
9. the described micro mist purification of any one process units according to claim 1 to 8, is characterized in that, be equiped with charging hopper on described charge door, the large end of charging hopper is in outside tank body, and the small end of charging hopper stretches in tank body.
10. the described micro mist purification of any one process units according to claim 1 to 8, is characterized in that, also offers on described tank body for the acid discharge mouth of discharging the acid solution after the flushing water dilution in tank body.
CN 201220692964 2012-12-15 2012-12-15 Micro powder purification production device Expired - Lifetime CN202984174U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220692964 CN202984174U (en) 2012-12-15 2012-12-15 Micro powder purification production device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220692964 CN202984174U (en) 2012-12-15 2012-12-15 Micro powder purification production device

Publications (1)

Publication Number Publication Date
CN202984174U true CN202984174U (en) 2013-06-12

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CN (1) CN202984174U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107225117A (en) * 2016-03-25 2017-10-03 内蒙古蒙牛乳业(集团)股份有限公司 The cleaning device and cleaning method of sea sand
CN109731846A (en) * 2019-02-13 2019-05-10 中钛集团焦作市裕盛钛业有限公司 Full-automatic elution instrument and its application method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107225117A (en) * 2016-03-25 2017-10-03 内蒙古蒙牛乳业(集团)股份有限公司 The cleaning device and cleaning method of sea sand
CN109731846A (en) * 2019-02-13 2019-05-10 中钛集团焦作市裕盛钛业有限公司 Full-automatic elution instrument and its application method
CN109731846B (en) * 2019-02-13 2021-12-31 中钛集团焦作市裕盛钛业有限公司 Full-automatic elution instrument and use method thereof

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C14 Grant of patent or utility model
GR01 Patent grant
ASS Succession or assignment of patent right

Owner name: HE'NAN FUNIK ULTRAHARD MATERIAL CO., LTD.

Effective date: 20141014

Owner name: HENAN FULAIGE ULTRAHARD MATERIAL CO., LTD.

Free format text: FORMER OWNER: HE'NAN FUNIK ULTRAHARD MATERIAL CO., LTD.

Effective date: 20141014

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 450001 ZHENGZHOU, HENAN PROVINCE TO: 454950 JIAOZUO, HENAN PROVINCE

TR01 Transfer of patent right

Effective date of registration: 20141014

Address after: Wu Wuzhi County route 454950 Henan province Ge Dang Village West

Patentee after: HENAN FULAIGE ULTRAHARD MATERIAL Co.,Ltd.

Patentee after: HENAN FUNIK ULTRAHARD MATERIAL Co.,Ltd.

Address before: 450001 Zhengzhou high tech Industrial Development Zone, Henan, Holly Street, No. 16

Patentee before: HENAN FUNIK ULTRAHARD MATERIAL Co.,Ltd.

C56 Change in the name or address of the patentee
CP01 Change in the name or title of a patent holder

Address after: Wu Wuzhi County route 454950 Henan province Ge Dang Village West

Patentee after: HENAN FULAIGE ULTRAHARD MATERIAL Co.,Ltd.

Patentee after: FUNIK ULTRAHARD MATERIAL Co.,Ltd.

Address before: Wu Wuzhi County route 454950 Henan province Ge Dang Village West

Patentee before: HENAN FULAIGE ULTRAHARD MATERIAL Co.,Ltd.

Patentee before: HENAN FUNIK ULTRAHARD MATERIAL Co.,Ltd.

CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20130612