CN202962299U - Mixing device of blending liquid for production of electrode foils - Google Patents
Mixing device of blending liquid for production of electrode foils Download PDFInfo
- Publication number
- CN202962299U CN202962299U CN 201220732340 CN201220732340U CN202962299U CN 202962299 U CN202962299 U CN 202962299U CN 201220732340 CN201220732340 CN 201220732340 CN 201220732340 U CN201220732340 U CN 201220732340U CN 202962299 U CN202962299 U CN 202962299U
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- distiller liquor
- produced
- electrode foil
- tank body
- mixing arrangement
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Abstract
The utility model discloses a mixing device of blending liquid for production of electrode foils. The mixing device comprises a tank (1) and a pump (2), wherein an inlet pipeline of the pump (2) is communicated to a circulating outlet (3) in the bottom end of the tank (1), and a outlet pipeline of the pump (2) is communicated to a circulating inlet (4) in the upper end of the tank (1). The mixing device of the blending liquid for the production of the electrode foils has the advantages that the liquid is pumped out from the lower end of the tank by using a centrifugal pump and then is pumped in from the upper end of the tank, so that the liquid in the tank is fully mixed; a leakage screen is arranged at the lower end of the circulating inlet, so that the liquid is divided, dispersed in a large scale and joined with the blending liquid at the lower part, thus accelerating the mixing speed; and a heating device is arranged at the circulating inlet, heat, lost n a circulating pipeline, of the blending liquid and heat radiating in the tank can be heated by the heating device, so that the temperature in the tank can reach the requirement, and the blending liquid is avoided being crystallized.
Description
Technical field
The utility model relates to apparatus for combining liquids, particularly relates to the mixing arrangement that a kind of electrode foil is produced distiller liquor.
Background technology
At present, the mixing of the distiller liquor during electrode foil is produced, the main mixer that adopts stirs, but adopt mixer to stir and have following defective: the shaft of (1) mixer, paddle are under corrosive electrolyte environment, add that production line passes the electricity of coming, easily electrochemical corrosion, cause iron ion increase in tank liquid, and follow-up Waste Acid From Hua Cheng Foil production is affected; (2) reasons such as the degree of depth of paddle, length, the distiller liquor that is positioned at bottom and sidewall is difficult to be stirred to, thereby causes the mixed effect of distiller liquor not reach requirement.
The utility model content
The purpose of this utility model is to overcome the shortcoming and defect of above-mentioned prior art, provide a kind of electrode foil to produce the mixing arrangement of distiller liquor, overcome the existing following defective that adopts the distiller liquor mixing arrangement of mixer: in mixed process, because the shaft of mixer, paddle directly contact with distiller liquor, easy electrochemical corrosion, thereby cause the iron ion in distiller liquor to increase, for subsequent production stays impact; And the distiller liquor of bottom and sidewall, paddle is difficult to be stirred to, and makes the mixed effect of distiller liquor undesirable.
The purpose of this utility model is achieved through the following technical solutions: electrode foil is produced the mixing arrangement of distiller liquor, comprise tank body and pump, the import of described pump is communicated to the loop exit of tank body bottom, its outlet is communicated to the circulation import of tank body upper end, after distiller liquor is put into tank body, pump is with the loop exit sucking-off of distiller liquor from the tank body bottom, and then with distiller liquor in circulation inlet pumps into tank body, the distiller liquor that has just entered just with tank body in distiller liquor carry out collisional mixing, so continuous sucking-off pumps into, and mixes thereby reach fully.
Being provided with one in tank body of the present utility model slips through the net, the described level of slipping through the net is installed, its height is lower than the height of circulation import, when distiller liquor enters in tank body from circulation inlet, namely need through slipping through the net, distiller liquor can be slipped through the net is divided into many parts, and be a wide range of dispersion, then fall with following distiller liquor and converge, make like this distiller liquor better be mixed, accelerated mixing velocity.
Circulation inlet of the present utility model is provided with a heater, because producing distiller liquor, the electrode foil in tank body generally need to maintain certain temperature, but distiller liquor is by circulating line (being the pipeline between loop exit and circulation import) time, heat will scatter and disappear, add a heater in circulation inlet, can guarantee the temperature in tank.
Further, be provided with a temperature inductor in tank body, the output of temperature inductor connects the control end of heater by a magnetic valve, the temperature that needs when temperature in tank is not less than the distiller liquor mixing is when (being called temperature limit), and heater can not worked.The utility model is by temperature in a temperature inductor induction tank, when temperature in tank during lower than temperature limit, temperature inductor namely transmits a signal to magnetic valve, then control heater and begin heating, when temperature in tank during higher than temperature limit, temperature inductor namely transmits a signal to magnetic valve, controls heater stop work, has saved like this electric energy.
Further, described heater comprises housing, be provided with heat exchanger channels in housing, heat exchanger channels is divided into two passages by partition panel, i.e. first passage and second channel, described first passage one end communication loop import, the other end is communicated with delivery side of pump, second channel is communicated with the external heating medium pipeline, and the import department of second channel is provided with an electrically operated valve, and the control end of described electrically operated valve is connected to magnetic valve.First passage is used for the circulation distiller liquor like this, and second channel is used for the circulation external heating medium, and regulator solution and heat medium carry out heat exchange by partition panel.In the time of general, electrically operated valve is closed condition, at this moment only has distiller liquor to pass through first passage, and heater uses as just pipeline; When temperature in tank during lower than temperature limit, temperature inductor namely transmits a signal to magnetic valve, the control electrically operated valve is opened, heat medium namely flows through second channel, with the isolating valve, of being separated by of the distiller liquor in first passage, heat medium and distiller liquor namely carry out exchange heat by isolating valve,, and the temperature of heat medium namely heats distiller liquor higher than distiller liquor.
Connecting pipe between the pump of the present embodiment and circulation import is provided with discharging opening, and discharging opening and circulation inlet all are provided with valve, and these two valves are used for switching and mix or discharging.During mixing, close the valve at discharging opening place, open the valve of circulation inlet, pump is with the loop exit sucking-off of distiller liquor from the tank body bottom, and then with distiller liquor in circulation inlet pumps into tank body, the distiller liquor that has just entered just with tank body in distiller liquor carry out collisional mixing; During discharging, close the valve of circulation inlet, open the valve at discharging opening place, start pump, be about to the interior distiller liquor of tank body from extracting rear use out.
Tank body of the present utility model bottom also is provided with discharge gate, the waste water that is used for discharging discarded distiller liquor or cleans tank body.
Pump of the present utility model is corrosion resistant centrifugal pump, and electrode foil is produced distiller liquor and had corrosivity, so pump need to be corrosion-resistant
Tank body of the present utility model adopts corrosion-resistant material to make, and adopts preferably polypropylene to make, and has corrosivity because electrode foil is produced distiller liquor.
The beneficial effects of the utility model are:
(1) adopt centrifugal pump to extract liquid out from the tank body lower end, then pump into from the tank body upper end, make like this liquid in tank body be mixed;
(2) arrange one in tank body circulation import lower end and slip through the net, make liquid divided, disperse on a large scale, converge with following distiller liquor, accelerated mixing velocity;
(3) in circulation inlet, a heater is set, distiller liquor is dispersed heat in circulating line, and the heat that dispels the heat in tank, can heat by heater, guarantees that the temperature in tank reaches requirement, avoids the distiller liquor crystallization.
Description of drawings
Fig. 1 is the structural representation of embodiment 1;
Fig. 2 is the structural representation of embodiment 2;
Fig. 3 is the structural representation of embodiment 3;
Fig. 4 is the structural representation of heater;
In figure, the 1-tank body, the 2-pump, the 3-loop exit, 4-circulation import, 5-slips through the net, 6-discharge gate, 7-discharging opening, 8-heater, 81-housing, 82-heat exchanger channels, 83-electrically operated valve, 84-partition panel, 85-first passage, 86-second channel.
The specific embodiment
The utility model is described in further detail below in conjunction with embodiment, but structure of the present utility model is not limited only to following examples:
[embodiment 1]
As shown in Figure 1, electrode foil is produced the mixing arrangement of distiller liquor, comprises tank body 1 and pump 2, and the inlet pipeline of described pump 2 is communicated to the loop exit 3 of tank body 1 bottom, and its outlet conduit is communicated to the circulation import 4 of tank body 1 upper end.
The pump 2 of the present embodiment and the connecting pipe between circulation import 4 are provided with discharging opening 7, and discharging opening 7 and circulation import 4 places all are provided with valve.
The pump 2 of the present embodiment is corrosion resistant centrifugal pump.
The tank body 1 of the present embodiment adopts corrosion-resistant material to make, adopt preferably polypropylene plastics, the import of pump 2 is to the pipeline between tank body 1 bottom loop exit 3, and the pipeline between the circulation import 4 that exports to tank body 1 upper end of pump 2 all adopts anticorrosive material to make.
[embodiment 2]
As Fig. 2, the structure of the structure of the present embodiment and embodiment 1 is basically identical, and difference is that being provided with one in described tank body 1 slips through the net 5, and described 5 levels of slipping through the net are installed, and its height is lower than the height of circulation import 4.
[embodiment 3]
As shown in Figure 3, Figure 4, the structure of the structure of the present embodiment and embodiment 1 is basically identical, difference be to circulate import 4 places are provided with a heater 8, heater 8 comprises housing 81, is provided with heat exchanger channels 82 in housing 81, and heat exchanger channels 82 is divided into two passages by partition panel 84, be first passage 85 and second channel 86, described first passage 85 1 end communication loop imports 4, the other end is communicated with the outlet of pump 2, and second channel 86 is communicated with the external heating medium pipeline.
The present embodiment arranges a temperature inductor tank body 1 is interior, in the import department of second channel 86, an electrically operated valve 83 is set, and the output of temperature inductor connects the control end of electrically operated valve 83 by a magnetic valve, control the work of electrically operated valve 83.
As above, can implement well the utility model.
Claims (10)
1. electrode foil is produced the mixing arrangement of distiller liquor, it is characterized in that, comprise tank body (1) and pump (2), the inlet pipeline of described pump (2) is communicated to the loop exit (3) of tank body (1) bottom, and its outlet conduit is communicated to the circulation import (4) of tank body (1) upper end.
2. electrode foil according to claim 1 is produced the mixing arrangement of distiller liquor, it is characterized in that, is provided with one slip through the net (5) in described tank body (1), and described slipping through the net (5) level is installed, and its height is lower than the height of circulation import (4).
3. electrode foil according to claim 1 is produced the mixing arrangement of distiller liquor, it is characterized in that, described circulation import (4) locates to be provided with a heater (8).
4. electrode foil according to claim 3 is produced the mixing arrangement of distiller liquor, it is characterized in that, is provided with a temperature inductor in described tank body (1), and the output of temperature inductor connects the control end of heater (8) by a magnetic valve.
5. electrode foil according to claim 4 is produced the mixing arrangement of distiller liquor, it is characterized in that, described heater (8) comprises housing (81), be provided with heat exchanger channels (82) in housing (81), heat exchanger channels (82) is divided into two passages by partition panel (84), be first passage (85) and second channel (86), described first passage (85) one end communication loop imports (4), the other end is communicated with the outlet of pump (2), second channel (86) is communicated with the external heating medium pipeline, the import department of second channel (86) is provided with an electrically operated valve (83), the control end of described electrically operated valve (83) is connected to magnetic valve.
6. electrode foil according to claim 1 is produced the mixing arrangement of distiller liquor, it is characterized in that, the connecting pipe between described pump (2) and circulation import (4) is provided with discharging opening (7).
7. electrode foil according to claim 3 is produced the mixing arrangement of distiller liquor, it is characterized in that, described discharging opening (7) locates to be provided with valve.
8. electrode foil according to claim 1 is produced the mixing arrangement of distiller liquor, it is characterized in that, described circulation import (4) locates to be provided with valve.
9. electrode foil according to claim 1 is produced the mixing arrangement of distiller liquor, it is characterized in that, described tank body (1) bottom also is provided with discharge gate (6).
10. electrode foil according to claim 1 is produced the mixing arrangement of distiller liquor, it is characterized in that, described pump (2) is corrosion resistant centrifugal pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220732340 CN202962299U (en) | 2012-12-27 | 2012-12-27 | Mixing device of blending liquid for production of electrode foils |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220732340 CN202962299U (en) | 2012-12-27 | 2012-12-27 | Mixing device of blending liquid for production of electrode foils |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202962299U true CN202962299U (en) | 2013-06-05 |
Family
ID=48503430
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220732340 Expired - Fee Related CN202962299U (en) | 2012-12-27 | 2012-12-27 | Mixing device of blending liquid for production of electrode foils |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202962299U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106040033A (en) * | 2016-07-25 | 2016-10-26 | 湖北鑫统领万象科技有限公司 | Storage tank for blending of grinding aids |
| CN106861485A (en) * | 2017-03-03 | 2017-06-20 | 吉姆西半导体科技（无锡）有限公司 | Chemical liquid feed system and supply method |
| CN112180033A (en) * | 2019-07-04 | 2021-01-05 | 西安西电开关电气有限公司 | Gas mixing device and gas mixing method |
-
2012
- 2012-12-27 CN CN 201220732340 patent/CN202962299U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106040033A (en) * | 2016-07-25 | 2016-10-26 | 湖北鑫统领万象科技有限公司 | Storage tank for blending of grinding aids |
| CN106861485A (en) * | 2017-03-03 | 2017-06-20 | 吉姆西半导体科技（无锡）有限公司 | Chemical liquid feed system and supply method |
| CN112180033A (en) * | 2019-07-04 | 2021-01-05 | 西安西电开关电气有限公司 | Gas mixing device and gas mixing method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130605 Termination date: 20141227 |
|
| EXPY | Termination of patent right or utility model |