CN207591306U - One kind is used for evaporation and crystal process slurry automatic discharge device - Google Patents
One kind is used for evaporation and crystal process slurry automatic discharge device Download PDFInfo
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- CN207591306U CN207591306U CN201721657531.3U CN201721657531U CN207591306U CN 207591306 U CN207591306 U CN 207591306U CN 201721657531 U CN201721657531 U CN 201721657531U CN 207591306 U CN207591306 U CN 207591306U
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- Prior art keywords
- crystallizer
- communicated
- discharge nozzle
- cyclone
- discharge
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- 238000000034 method Methods 0.000 title claims abstract description 20
- 239000002002 slurry Substances 0.000 title claims abstract description 16
- 238000001704 evaporation Methods 0.000 title claims abstract description 15
- 239000013078 crystal Substances 0.000 title claims abstract description 14
- 230000008020 evaporation Effects 0.000 title claims abstract description 14
- 238000007599 discharging Methods 0.000 claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000010992 reflux Methods 0.000 claims description 18
- 239000000945 filler Substances 0.000 claims description 9
- 238000002425 crystallisation Methods 0.000 claims description 5
- 230000008025 crystallization Effects 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 8
- 239000007788 liquid Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 230000000903 blocking effect Effects 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003550 marker Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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- Cyclones (AREA)
Abstract
The utility model discloses one kind to be used for evaporation and crystal process slurry automatic discharge device, including crystallizer, the bottom of the crystallizer is communicated with the first discharge nozzle, the described one end of first discharge nozzle far from crystallizer is communicated with discharging pump, the water outlet of the discharging pump is communicated with the second discharge nozzle, the described one end of second discharge nozzle far from discharging pump is communicated with cyclone, the bottom of the cyclone is communicated with third discharge nozzle, electromagnetic flowmeter is provided on the left of the third discharging pipe surface, the surface of the third discharge nozzle and electric control valve is provided on the right side of the electromagnetic flowmeter.The utility model is by setting crystallizer, discharging pump, cyclone, electromagnetic flowmeter and electric control valve, controllable magma is automatically drained out, and pipeline is not easy to plug in discharge process, the time of discharge can not only be controlled, and the amount of discharge can be controlled, it is convenient for people to the production to magma.
Description
Technical field
The utility model is related to magma technical field of processing equipment, specially a kind of automatic for evaporation and crystal process slurry
Discharger.
Background technology
In small-sized MVR evaporation and crystal processes, the magma feed liquid containing crystallization is easily blocked from vapo(u)rization system discharge process
Pipeline, and the condition of high temperature, scale removal process is very inconvenient, this secondary design one kind is used for small-sized evaporation and crystal process slurry interval certainly
Dynamic discharger, in small vapo(u)rization system, the concentrate load containing crystallization is smaller, in design, if marker pipe is set
Meter is too big, and such flow velocity is low, and the flow for crystallizing discharging is difficult to control, if discharge pipe design is too small, although discharging flow
Size controls well, but is easily blocked on discharge nozzle road, and system can not just be run, thus it is proposed that a kind of tie for evaporating
Brilliant process slurry automatic discharge device.
Invention content
The purpose of this utility model is to provide one kind for evaporation and crystal process slurry automatic discharge device, have and be not easy
Blocking pipeline, and have the advantages of can accurately controlling discharging flow, solve easy blocking pipeline, and can not accurately control
The problem of discharging flow.
To achieve the above object, the utility model provides following technical solution：One kind is used for evaporation and crystal process slurry certainly
Dynamic discharger, including crystallizer, the bottom of the crystallizer is communicated with the first discharge nozzle, and first discharge nozzle is far from crystallization
One end of device is communicated with discharging pump, and the water outlet of the discharging pump is communicated with the second discharge nozzle, and second discharge nozzle is far from going out
One end of material pump is communicated with cyclone, and the bottom of the cyclone is communicated with third discharge nozzle, the third discharging pipe surface
Left side is provided with electromagnetic flowmeter, the surface of the third discharge nozzle and is provided with motorized adjustment on the right side of electromagnetic flowmeter
Valve.
Preferably, filler pipe is communicated on the right side of the crystallizer, the filler pipe is located at the axle center on the right side of crystallizer.
Preferably, be fixedly connected with reflux pump at the top of the cyclone, the water inlet of the reflux pump by pipeline with
Cyclone connects, and the water outlet of the reflux pump is communicated with return duct, the return duct one end and crystallizer far from reflux pump
Connection.
Preferably, the cross-sectional area of the crystallizer and cyclone apex is all higher than the rank street area of bottom.
Compared with prior art, the beneficial effects of the utility model are as follows：
1st, the utility model is by setting crystallizer, discharging pump, cyclone, electromagnetic flowmeter and electric control valve, controllably
Combinations slurry is automatically drained out, and pipeline is not easy to plug in discharge process, not only the time of discharge can be controlled, Er Qieke
The amount of discharge is controlled, is convenient for people to the production to magma.
2nd, the utility model fills magma in crystallizer, avoids the occurrence of the very few situation of magma by filler pipe, convenience,
By the first discharge nozzle, achieve the effect that connect crystallizer and discharging pump, facilitate and magma is sucked out, pass through reflux pump and reflux
Pipe, achievees the effect that make clear liquid in cyclone to flow back into crystallizer, while be also convenient for material in pipeline and circulated, is not easy
It results in blockage to pipeline, by third discharge nozzle, achievees the effect that discharge magma, by electromagnetic flowmeter, reach to flow
The effect of control avoids the occurrence of and discharges excessive or very few situation, and by electric control valve, the time that magma is discharged can be carried out
Control, avoids the occurrence of the situation that can not be discharged.
Description of the drawings
FIG. 1 is a schematic structural view of the utility model.
In figure：1 crystallizer, 2 first discharge nozzles, 3 discharging pumps, 4 second discharge nozzles, 5 cyclones, 6 third discharge nozzles, 7 electricity
Magnetic flowmeter, 8 electric control valves, 9 filler pipes, 10 reflux pumps, 11 return ducts.
Specific embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
It clearly and completely describes, it is clear that the described embodiments are only a part of the embodiments of the utility model rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are without making creative work
All other embodiments obtained shall fall within the protection scope of the present invention.
Referring to Fig. 1, a kind of for evaporation and crystal process slurry automatic discharge device, including crystallizer 1, in crystallizer 1
Magma be pumped into cyclone 5 by discharging pump 3, can make to have in pipeline a large amount of Matter Transfer to flow in this way, pipeline is not easy out
It now blocks, the right side of crystallizer 1 is communicated with filler pipe 9, and by filler pipe 9, the convenient filling magma in crystallizer 1 avoids out
The very few situation of existing magma, filler pipe 9 are located at the axle center on 1 right side of crystallizer, the cross section at 5 top of crystallizer 1 and cyclone
Product is all higher than the rank street area of bottom, and the bottom of crystallizer 1 is communicated with the first discharge nozzle 2, by the first discharge nozzle 2, reaches company
The effect of crystallizer 1 and discharging pump 3 is connect, facilitates and magma is sucked out, first one end of discharge nozzle 2 far from crystallizer 1 is communicated with out
Material pump 3, the water outlet of discharging pump 3 is communicated with the second discharge nozzle 4, and second one end of discharge nozzle 4 far from discharging pump 3 is communicated with eddy flow
Device 5, the crystallization inside cyclone 5 are settled down to bottom, and clear liquid is discharged by reflux pump 10 and return duct 11 in crystallizer 1, eddy flow
The top of device 5 is fixedly connected with reflux pump 10, and the water inlet of reflux pump 10 is connected by pipeline with cyclone 5, reflux pump 10
Water outlet is communicated with return duct 11, and the one end of return duct 11 far from reflux pump 10 is connected with crystallizer 1, by reflux pump 10 and returns
Flow tube 11 achievees the effect that make clear liquid in cyclone 5 to flow back into crystallizer 1, while is also convenient for material in pipeline and carries out recycle stream
It is dynamic, it is not easy to result in blockage to pipeline, the bottom of cyclone 5 is communicated with third discharge nozzle 6, and by third discharge nozzle 6, reaching will be brilliant
The effect of discharge is starched, third discharge nozzle is provided with electromagnetic flowmeter 7 on the left of 6 surface, by electromagnetic flowmeter 7, reaches convection current
The effect of control is measured, avoids the occurrence of the excessive or very few situation of discharging, the surface of third discharge nozzle 6 and positioned at electromagnetic flowmeter 7
Right side be provided with electric control valve 8, electric control valve 8 was opened once every 10 minutes intervals, under the impact of big flow, can will
The magma of 5 bottom of cyclone is all discharged, and by electric control valve 8, the time that can be discharged to magma controls, avoids the occurrence of
The situation that can not be discharged, by setting crystallizer 1, discharging pump 3, cyclone 5, electromagnetic flowmeter 7 and electric control valve 8, controllably
Combinations slurry is automatically drained out, and pipeline is not easy to plug in discharge process, not only the time of discharge can be controlled, Er Qieke
The amount of discharge is controlled, is convenient for people to the production to magma.
In use, discharging pump 3 is pumped out the magma in crystallizer 1 by the first discharge nozzle 2, pumped by the second discharge nozzle 4
Enter in cyclone 5, the clear liquid in cyclone 5 is discharged by return duct 11 in crystallizer 1 and is processed by reflux pump 10, and magma leads to
It crosses cyclone 5 and carries out storage processing, electric control valve 8 is run, and magma is discharged by third discharge nozzle 6, simultaneously also by electromagnetism
Flowmeter 7 controls the amount of discharge, and the amount of discharge is 500kg/h.
In summary：This is used for evaporation and crystal process slurry automatic discharge device, passes through crystallizer 1, discharging pump 3, eddy flow
The cooperation of device 5, electromagnetic flowmeter 7 and electric control valve 8 solves easy blocking pipeline, and can not accurately control reactor effluent stream
The problem of amount.
While there has been shown and described that the embodiment of the utility model, for the ordinary skill in the art,
It is appreciated that can these embodiments be carried out with a variety of variations in the case of the principle and spirit for not departing from the utility model, repaiied
Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.
Claims (4)
1. one kind is for evaporation and crystal process slurry automatic discharge device, including crystallizer（1）, it is characterised in that：The crystallization
Device（1）Bottom be communicated with the first discharge nozzle（2）, first discharge nozzle（2）Far from crystallizer（1）One end be communicated with discharging
Pump（3）, the discharging pump（3）Water outlet be communicated with the second discharge nozzle（4）, second discharge nozzle（4）Far from discharging pump（3）
One end be communicated with cyclone（5）, the cyclone（5）Bottom be communicated with third discharge nozzle（6）, the third discharge nozzle
（6）Electromagnetic flowmeter is provided on the left of surface（7）, the third discharge nozzle（6）Surface and positioned at electromagnetic flowmeter（7）'s
Right side is provided with electric control valve（8）.
It is 2. according to claim 1 a kind of for evaporation and crystal process slurry automatic discharge device, it is characterised in that：It is described
Crystallizer（1）Right side be communicated with filler pipe（9）, the filler pipe（9）Positioned at crystallizer（1）At the axle center on right side.
It is 3. according to claim 1 a kind of for evaporation and crystal process slurry automatic discharge device, it is characterised in that：It is described
Cyclone（5）Top be fixedly connected with reflux pump（10）, the reflux pump（10）Water inlet pass through pipeline and cyclone（5）
Connection, the reflux pump（10）Water outlet be communicated with return duct（11）, the return duct（11）Far from reflux pump（10）One
End and crystallizer（1）Connection.
It is 4. according to claim 1 a kind of for evaporation and crystal process slurry automatic discharge device, it is characterised in that：It is described
Crystallizer（1）And cyclone（5）The cross-sectional area at top is all higher than the rank street area of bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721657531.3U CN207591306U (en) | 2017-12-03 | 2017-12-03 | One kind is used for evaporation and crystal process slurry automatic discharge device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721657531.3U CN207591306U (en) | 2017-12-03 | 2017-12-03 | One kind is used for evaporation and crystal process slurry automatic discharge device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207591306U true CN207591306U (en) | 2018-07-10 |
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ID=62762132
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721657531.3U Active CN207591306U (en) | 2017-12-03 | 2017-12-03 | One kind is used for evaporation and crystal process slurry automatic discharge device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207591306U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109045745A (en) * | 2018-08-10 | 2018-12-21 | 国家海洋局天津海水淡化与综合利用研究所 | A kind of band promotes the continuous vacuum equipment of crystallisation by cooling of water conservancy diversion |
-
2017
- 2017-12-03 CN CN201721657531.3U patent/CN207591306U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109045745A (en) * | 2018-08-10 | 2018-12-21 | 国家海洋局天津海水淡化与综合利用研究所 | A kind of band promotes the continuous vacuum equipment of crystallisation by cooling of water conservancy diversion |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: No. 1-3, Lane 369, Changshi Road, Sijing Town, Songjiang District, Shanghai, 201600 Patentee after: Shanghai Zhongteng Equipment Technology Co.,Ltd. Country or region after: China Address before: 151 Wangdong Middle Road, Sijing Town, Songjiang District, Shanghai, 20101 Patentee before: SHANGHAI ZHONGTENG ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Country or region before: China |