CN207025177U - A kind of dissolver in molysite production process - Google Patents
A kind of dissolver in molysite production process Download PDFInfo
- Publication number
- CN207025177U CN207025177U CN201720826487.8U CN201720826487U CN207025177U CN 207025177 U CN207025177 U CN 207025177U CN 201720826487 U CN201720826487 U CN 201720826487U CN 207025177 U CN207025177 U CN 207025177U
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- Prior art keywords
- dissolving tank
- dissolver
- molysite
- production process
- dissolving
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 24
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 title claims abstract description 18
- 239000007788 liquid Substances 0.000 claims abstract description 29
- 239000012530 fluid Substances 0.000 claims abstract description 18
- 239000000463 material Substances 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 238000005253 cladding Methods 0.000 claims abstract description 8
- 239000004744 fabric Substances 0.000 claims description 10
- 238000007599 discharging Methods 0.000 abstract description 8
- 238000003756 stirring Methods 0.000 abstract description 8
- 238000009825 accumulation Methods 0.000 abstract description 4
- 239000002245 particle Substances 0.000 description 16
- 239000007787 solid Substances 0.000 description 13
- 239000011343 solid material Substances 0.000 description 12
- 238000004090 dissolution Methods 0.000 description 9
- 230000009286 beneficial effect Effects 0.000 description 5
- 230000000903 blocking effect Effects 0.000 description 4
- 238000010276 construction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000009527 percussion Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
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- Filtration Of Liquid (AREA)
Abstract
A kind of dissolver in molysite production process, including dissolving tank, charging aperture and water inlet are respectively equipped with dissolving tank, is provided with screen mesh groove in dissolving tank, the side and bottom surface of screen mesh groove have space between dissolving tank, the top of dissolving tank is provided with support body, support body is provided with motor, and the lower end of motor is provided with rotary shaft, and rotary shaft is provided with stirring vane, rotary shaft and rotating vane are in screen mesh groove, and screen mesh groove upper end is fixedly connected with support body；Dissolving tank is connected with fluid reservoir by connecting pipe, and connecting pipe is provided with the first liquid pump, is provided with the first thin filter of cladding connecting pipe end in dissolving tank with the junction in connecting pipe.The utility model can not only realize quick dissolving, moreover it is possible to effectively avoid the accumulation of material and block discharging opening.
Description
Technical field
It the utility model is related to a kind of dissolver, the dissolver in particularly a kind of molysite production process.
Background technology
Raw materials for production addition solvent in process of production, can be dissolved into liquid condition by molysite using dissolver in advance,
It is then store in storage tank, is so easy to the orderly progress of production process.Existing dissolver be mostly fixed square groove type or
The dissolving tank of cylindrical type, the needs that subsequent production is supplied after different concentration are dissolved into it, existing dissolver is in dissolving
During often occur solid material accumulation situation, it is impossible in time dissolving, and easily block dissolving tank discharging opening, occur
Artificial treatment is carried out, it is necessary to stop operation after this situation, production disruption is easily caused, wastes time and energy, can also increase production cost.
CN204768310U discloses a kind of dissolver, and it includes dissolving tank, also includes being placed on by branch in composition
The fluid reservoir of screen mesh groove and connection dissolving tank in dissolving tank, the upper end of the dissolving tank are provided with charging aperture, and lower end is provided with discharging
Mouthful, charging aperture connects fluid reservoir with discharge pipe by feed pipe respectively with discharging opening, centrifugal pump is connected with discharge pipe,
The utility model sets porous screen mesh groove on dissolving tank, increases the contact area of material and solvent, can promote the molten of material
Solution, avoid the accumulation of material and further block discharging opening, a large amount of continuous-dissolutions of material can be achieved, improve production efficiency
And labor intensity is reduced, but the utility model can cause molten because solid material is nearly at inactive state in screen mesh groove
It is slower to solve speed, and the screen mesh groove of the utility model can only also stop the larger solid material of some particles, for some grains
Footpath is smaller and has little time the material dissolved, still can there is the possibility for blocking dissolving tank discharging opening.
The content of the invention
The purpose of this utility model is to overcome the above-mentioned deficiency of prior art and provide molten in a kind of molysite production process
Device is solved, it can not only realize quick dissolving, moreover it is possible to effectively avoid the accumulation of material and block discharging opening.
The technical solution of the utility model is：A kind of dissolver in molysite production process, including dissolving tank, dissolving tank
On be respectively equipped with charging aperture and water inlet, is provided with screen mesh groove in dissolving tank, the side and bottom surface of screen mesh groove are between dissolving tank
Space be present, the top of dissolving tank is provided with support body, and support body is provided with motor, and the lower end of motor is provided with rotary shaft, rotation
Rotating shaft is provided with stirring vane, and rotary shaft and rotating vane are in screen mesh groove, and screen mesh groove upper end is fixedly connected with support body；Dissolving
Groove is connected with fluid reservoir by connecting pipe, and connecting pipe is provided with the first liquid pump, and the first liquid pump is easy in dissolving tank
Obtained solution is transferred in fluid reservoir, and the of cladding connecting pipe end is provided with the junction in connecting pipe in dissolving tank
One thin filter.
Appropriate clear water is added into dissolving tank by water inlet, solid material in dissolving tank is entered by charging aperture,
Drop into screen mesh groove and dissolved first, during rotary shaft drives stirring vane rotation, the thing in screen mesh groove can be made
Material is quickly dissolved, although as the diameter of the progress solid material of course of dissolution can taper into, and then screen cloth can be passed through
Groove drops into dissolving trench bottom, but the presence of screen mesh groove does not interfere with the perturbation action of stirring vane, and stirring vane will can fall
Enter in the rapid dissolution phase for rolling participation again to the solid particle of dissolving trench bottom, the effect of screen mesh groove is both that placement is larger
Solid particle be not easy to be stirred blade and roll, and can reaches the phenomenon that solid particle realizes layering dissolving, beneficial to accelerating to dissolve
Speed, the first thin filter can effectively prevent the solid particle in solution tank through screen mesh groove from entering in connecting pipe and blocking up
Connecting pipe is filled in,, can be with liquid because its particle diameter is smaller for the solid particle of the very small diameter through the first thin filter
Flow process in dissolve, therefore will not also block connecting pipe.
The further technical scheme of the utility model is：It is always high that the link position of connecting pipe and dissolving tank is located at dissolving tank
Degree more than 1/2 is located, and the solid particle for ensureing to drop into dissolving tank bottom will not be assembled in connecting pipe end, ensures the company of entering
Fluid flow in threading a pipe is larger, and can reduce the minimum solid particle entered in connecting pipe, makes the molten of solid particle
Solution preocess is occurred mainly in dissolving tank.
Further, the bottom of fluid reservoir is connected by circulating line with dissolving tank bottom, circulating line and fluid reservoir, is connected
Pipeline collectively constitutes circulating path, beneficial to the flowing for promoting dissolving tank liquid, and then promotes accelerating for course of dissolution, circulates
Pipeline is provided with valve and second liquid pump, at the end of course of dissolution, valve can be closed, beneficial to the solution in dissolving tank is complete
Portion is transferred in fluid reservoir and stored, and second liquid pump quickly flows beneficial to liquid in circulating line.
Further, second thin mistake of the circulating line with being provided with cladding circulating line end in the dissolving tank of dissolving tank junction
Device is filtered, although in normal course of dissolution, the liquid in general solution tank will not be entered directly into circulating line, but logical
Cross connecting pipe and fluid reservoir is entered back into circulating line, but when stopping second liquid pump suddenly（Second liquid pump is sent out
During raw failure）, it is possible to phenomena such as suck-back occurs and cause the liquid in dissolving tank to enter directly into circulating line, due to molten
The tiny solid material of trench bottom meeting depositing dosed quantities is solved, so if being not provided with the second thin filter, solid particle be present
The possibility entered with liquid in circulating line, the second thin filter are the filter that permeable cloth or sieve diameter are not more than 0.5mm
Net, 0.5mm solid material is less than for particle diameter, can flow with liquid typically under the proper flow of liquid and easily move,
Therefore after second liquid pump is resumed work, this fraction solids particle can be re-introduced into dissolving tank or in circulating line
Dissolve, will not also produce the phenomenon for blocking circulating line.
Further, circulating line is parallel with the junction circulating line of dissolving tank is deep into the segment distance of dissolving tank one, the section
The length of distance is not more than the 1/15 of dissolving tank overall width, ensures that circulating line had not both interfered with the molten of solid material in dissolving tank
Solution preocess, and can produce parallel to dissolving trench bottom impulsive force, the impulsive force can auxiliary agitation blade will sink to dissolving tank
The object material of bottom is rolled and dissolved again.
Further, the first thin filter is not more than 0.2mm filter screen, simple in construction, energy for permeable cloth or sieve diameter
Reach preferable thin filter effect, be easily installed fixation（Only need to be coated on connecting pipe end using steel wire）.
Further, feed hopper is provided with charging aperture, is provided with material belt conveyor above feed hopper, water inlet goes out to be communicated with band
Valvular water tank, it is easy to implement the continued dissolution of a large amount of materials.
Further, fluid reservoir is provided with liquid taking port, passes through the liquid dissolved in liquid taking port convenient use fluid reservoir.
Further, dissolving tank and screen mesh groove are cylindrical structural, and screen cloth trench bottom is with dissolving the distance between trench bottom
To dissolve the 1/6-1/4 of groove height, guarantee, which is dropped between the solid material upper end of dissolving trench bottom and screen mesh groove, has space,
It is easy to drop into mobile dissolving of the solid material of dissolving trench bottom in dissolving tank.
Further, screen cloth groove sidewall is easy to dissolve with dissolving the 1/8-1/5 that the distance between groove sidewall is dissolving tank diameter
Tank liquid and solid material carry out free transfer between screen mesh groove and dissolving tank, and then are easy to the generation of vortex phenomenon, enter
And beneficial to quickening course of dissolution.
The utility model has following features compared with prior art：（1）The utility model in screen mesh groove by setting
The rotary shaft of stirring vane is carried, by the disturbance of stirring vane, the solid material that can make to fall into screen mesh groove quickly dissolves；
, can be by going out in circulating line additionally by being deep into circulating line is parallel with the access port of dissolving tank inside dissolving tank lower end
The circulating liquid come produces percussion to the fine solid particles of dissolving tank bottom precipitation, further makes to precipitate through screen mesh groove
Solid particle to dissolving trench bottom obtains the chance of secondary dissolving and realizes and be completely dissolved, so as to ensure the thing of dissolving tank everywhere
Material is respectively provided with higher rate of dissolution；（2）The utility model is provided with the dissolving tank of connecting pipe and the contact position of dissolving tank
The first thin filter of connecting pipe is coated, and is followed in the dissolving tank of circulating line and the contact position of dissolving tank provided with cladding
The second thin filter in endless tube road, it is ensured that enter in the liquid in connecting pipe and circulating line the solid particle contained
Thing is small-sized, can be completely dissolved completely with the flowing of liquid, and the phenomenon for blocking discharging opening may not occur.
Detailed construction of the present utility model is further described below in conjunction with the drawings and specific embodiments.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
As shown in drawings：A kind of dissolver in molysite production process, including dissolving tank 1, it is respectively equipped with dissolving tank 1
Charging aperture 1-1 and water inlet 1-2, dissolving tank 1 is interior to be provided with screen mesh groove 2, and the side and bottom surface of screen mesh groove 2 are between dissolving tank 1
Space be present, the top of dissolving tank 1 is provided with support body 3, and support body 3 is provided with motor 4, and the lower end of motor 4 is provided with rotation
Axle 5, rotary shaft 5 are provided with stirring vane 6, and rotary shaft 5 and rotating vane 6 are in screen mesh groove 2, the upper end of screen mesh groove 2 and support body 3
It is fixedly connected；Dissolving tank 1 is connected with fluid reservoir 8 by connecting pipe 7, and the link position of connecting pipe 7 and dissolving tank 1 is positioned at molten
The solution total height more than 1/2 of groove 1 is located, and fluid reservoir 8 is provided with liquid taking port 8-1, and connecting pipe 7 is provided with the first liquid pump 9, dissolving tank
The first thin filter 10 of cladding connecting pipe 7 end, the first thin filtering dress are provided with 1 with the junction in connecting pipe 7
It is permeable cloth to put 10.
The bottom of fluid reservoir 8 is connected by circulating line 11 with the bottom of dissolving tank 1, and circulating line 11 is provided with the He of valve 12
Second liquid pump 13；Circulating line 11 is with being provided with the second of cladding circulating line 11 end in the dissolving tank 1 of the junction of dissolving tank 1
Thin filter 14, the second thin filter 14 is the filter screen that sieve diameter is 0.5mm；The company of circulating line 11 and dissolving tank 1
The place's of connecing circulating line 11 is parallel to be deep into the segment distance of dissolving tank 1 one, and the length of the segment distance is not more than the 1/ of the overall width of dissolving tank 1
15。
Feed hopper 15 is provided with charging aperture 1-1, the top of feed hopper 15 is provided with material belt conveyor 16, and water inlet 1-2 goes out to connect
It is connected with valvular water tank 17.
Dissolving tank 1 and screen mesh groove 2 are cylindrical structural, and the distance between the bottom of screen mesh groove 2 and the bottom of dissolving tank 1 are molten
The 1/5 of the height of groove 1 is solved, the distance between the side wall of screen mesh groove 2 and the side wall of dissolving tank 1 are the 1/6 of the diameter of dissolving tank 1.
Claims (10)
1. the dissolver in a kind of molysite production process, including dissolving tank, charging aperture and water inlet are respectively equipped with dissolving tank,
Screen mesh groove is provided with dissolving tank, the side and bottom surface of screen mesh groove have space between dissolving tank, it is characterised in that：Dissolving tank
Top be provided with support body, support body is provided with motor, and the lower end of motor is provided with rotary shaft, and rotary shaft is provided with paddle
Piece, rotary shaft and rotating vane are in screen mesh groove, and screen mesh groove upper end is fixedly connected with support body；Dissolving tank is connected by connecting pipe
Fluid reservoir is connected to, connecting pipe is provided with the first liquid pump, and being provided with cladding with the junction in connecting pipe in dissolving tank connects
First thin filter of pipe end.
2. the dissolver in molysite production process according to claim 1, it is characterised in that：Connecting pipe and dissolving tank
Link position be located at dissolving tank total height more than 1/2 and locate.
3. the dissolver in molysite production process according to claim 1, it is characterised in that：The bottom of fluid reservoir passes through
Circulating line connects with dissolving tank bottom, and circulating line is provided with valve and second liquid pump.
4. the dissolver in molysite production process according to claim 3, it is characterised in that：Circulating line and dissolving tank
Be provided with the second thin filter of cladding circulating line end in the dissolving tank of junction, the second thin filter be permeable cloth or
Sieve diameter is not more than 0.5mm filter screen.
5. the dissolver in molysite production process according to claim 3, it is characterised in that：Circulating line and dissolving tank
Junction circulating line it is parallel be deep into the segment distance of dissolving tank one, the length of the segment distance is not more than the 1/ of dissolving tank overall width
15。
6. the dissolver in molysite production process according to any one of claim 1-5, it is characterised in that：First is thin
Filter is the filter screen that permeable cloth or sieve diameter are not more than 0.2mm.
7. the dissolver in molysite production process according to any one of claim 1-5, it is characterised in that：Charging aperture
Place is provided with feed hopper, is provided with material belt conveyor above feed hopper, water inlet, which goes out, to be communicated with valvular water tank.
8. the dissolver in molysite production process according to any one of claim 3-5, it is characterised in that：Fluid reservoir
It is provided with liquid taking port.
9. the dissolver in molysite production process according to any one of claim 1-5, it is characterised in that：Dissolving tank
It is cylindrical structural with screen mesh groove, screen cloth trench bottom is with dissolving 1/6-1/4 of the distance between the trench bottom for dissolving groove height.
10. the dissolver in molysite production process according to claim 9, it is characterised in that：Screen cloth groove sidewall with it is molten
Solve the 1/8-1/5 that the distance between groove sidewall is dissolving tank diameter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720826487.8U CN207025177U (en) | 2017-07-10 | 2017-07-10 | A kind of dissolver in molysite production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720826487.8U CN207025177U (en) | 2017-07-10 | 2017-07-10 | A kind of dissolver in molysite production process |
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| Publication Number | Publication Date |
|---|---|
| CN207025177U true CN207025177U (en) | 2018-02-23 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720826487.8U Active CN207025177U (en) | 2017-07-10 | 2017-07-10 | A kind of dissolver in molysite production process |
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| Country | Link |
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| CN (1) | CN207025177U (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108579478A (en) * | 2018-05-10 | 2018-09-28 | 重庆市永川区天堂化工厂 | Pesticide extraction element for pesticide producing |
| CN110104802A (en) * | 2019-04-17 | 2019-08-09 | 河南中烟工业有限责任公司 | A kind of water softening system dissolved salt device |
| CN110743228A (en) * | 2019-12-09 | 2020-02-04 | 山东东禾农业科技有限公司 | Solid-liquid circulating dissolving-mixing multistage filter and use method thereof |
| CN111485109A (en) * | 2020-04-21 | 2020-08-04 | 斯瑞尔环境科技股份有限公司 | Corridor type waste alloy cutter head dissolving device and dissolving method thereof |
| CN111773939A (en) * | 2020-06-02 | 2020-10-16 | 贵州中烟工业有限责任公司 | a salt pool |
| CN112575205A (en) * | 2021-01-05 | 2021-03-30 | 宁都县赣锋锂业有限公司 | Device and method for continuously leaching lithium sulfate from spodumene acid clinker |
| CN115845715A (en) * | 2022-12-20 | 2023-03-28 | 浙江新乐纺织化纤有限公司 | Saline-alkali solution saturation material device |
| CN116651372A (en) * | 2023-07-04 | 2023-08-29 | 四川红华实业有限公司 | Fluorination treatment device for unstable end group of fluorothermoplastic polymer |
| CN119345734A (en) * | 2024-12-04 | 2025-01-24 | 国药集团威奇达药业有限公司 | A laboratory crystallization device |
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2017
- 2017-07-10 CN CN201720826487.8U patent/CN207025177U/en active Active
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108579478A (en) * | 2018-05-10 | 2018-09-28 | 重庆市永川区天堂化工厂 | Pesticide extraction element for pesticide producing |
| CN110104802A (en) * | 2019-04-17 | 2019-08-09 | 河南中烟工业有限责任公司 | A kind of water softening system dissolved salt device |
| CN110104802B (en) * | 2019-04-17 | 2022-02-25 | 河南中烟工业有限责任公司 | A demineralized water system salt dissolving device |
| CN110743228A (en) * | 2019-12-09 | 2020-02-04 | 山东东禾农业科技有限公司 | Solid-liquid circulating dissolving-mixing multistage filter and use method thereof |
| CN110743228B (en) * | 2019-12-09 | 2023-09-08 | 山东东禾农业科技有限公司 | A solid-liquid circulating miscible multi-stage filter and its use method |
| CN111485109A (en) * | 2020-04-21 | 2020-08-04 | 斯瑞尔环境科技股份有限公司 | Corridor type waste alloy cutter head dissolving device and dissolving method thereof |
| CN111773939A (en) * | 2020-06-02 | 2020-10-16 | 贵州中烟工业有限责任公司 | a salt pool |
| CN112575205A (en) * | 2021-01-05 | 2021-03-30 | 宁都县赣锋锂业有限公司 | Device and method for continuously leaching lithium sulfate from spodumene acid clinker |
| CN115845715A (en) * | 2022-12-20 | 2023-03-28 | 浙江新乐纺织化纤有限公司 | Saline-alkali solution saturation material device |
| CN116651372A (en) * | 2023-07-04 | 2023-08-29 | 四川红华实业有限公司 | Fluorination treatment device for unstable end group of fluorothermoplastic polymer |
| CN119345734A (en) * | 2024-12-04 | 2025-01-24 | 国药集团威奇达药业有限公司 | A laboratory crystallization device |
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