CN203999870U - Change into wire casing liquid and preheat consumption reduction system - Google Patents
Change into wire casing liquid and preheat consumption reduction system Download PDFInfo
- Publication number
- CN203999870U CN203999870U CN201420384320.7U CN201420384320U CN203999870U CN 203999870 U CN203999870 U CN 203999870U CN 201420384320 U CN201420384320 U CN 201420384320U CN 203999870 U CN203999870 U CN 203999870U
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Abstract
The utility model relates to formed aluminum foil technical field, it discloses one and has changed into wire casing liquid and preheat consumption reduction system, solves in conventional art changing into that the whole process of wire casing liquid heating is all that the electric energy consumption that adopts electrically heated mode to bring is large, cost is high and long-term electrically heated easily brings the problem of potential safety hazard.The utility model accesses one in original water-cooled tube the hot-water line that changes into distinctive cooling backwater, by the control of valve, utilize the hot water in hot-water line through heat exchanger, tank liquor to be preheated, when being heated to after preset value, close hot-water line, switch to electrically heated; So can reduce the use of electric energy, cost-saving, and because the time of electricity consumption greatly reduces, also reduced the potential safety hazard in production process.The utility model is applicable to formed aluminum foil and produces energy-saving and cost-reducing.
Description
Technical field
The utility model relates to formed aluminum foil technical field, is specifically related to change into wire casing liquid and preheats consumption reduction system.
Background technology
Waste Acid From Hua Cheng Foil is mainly the anode foils being used in aluminium electrolutic capacitor, the whole process changing into is a kind of thermopositive reaction, it is in certain density tank liquor, in certain temperature, under certain reaction times, aluminium foil is applied to set voltage one by one, thereby form one deck densification, certain thickness γ '-Al2O3 at aluminium foil surface.The structure that changes into the whole Production Flow Chart of line comprises: put paper tinsel machine-charging roller-electrolyzer-liquid to major partss such as electric groove-electrolyzer-treatment trough-roasting furnace-foil closing machines.Auxiliary facility structure has: liquid-supplying system, cooling recirculation system, water manufacturing system, power supply system, Sewage treatment systems, ventilation system etc.At present, all to adopt electric heating tube to heat tank liquor in groove to changing into the whole process of wire casing liquid heating, and because of volume of bath solution larger, the constant temperature value that technology controlling and process requires is higher, so the electric energy consumption to the heating of tank liquor entirety is very large, particularly many change into line and heat simultaneously, have increased especially integral load, have limited to the line number of start simultaneously.
Therefore, in conventional art, all adopt electrically heated mode can directly increase cost input to changing into the whole process of wire casing liquid heating, and also easily bring the potential safety hazard in production with electrically heated for a long time.
Utility model content
Technical problem to be solved in the utility model is: propose one and change into wire casing liquid and preheat consumption reduction system, adopt this system can solve in conventional art changing into that the whole process of wire casing liquid heating is all that the electric energy consumption that adopts electrically heated mode to bring is large, cost is high and long-term electrically heated easily brings the problem of potential safety hazard.
The utility model solves the problems of the technologies described above adopted technical scheme:
Change into wire casing liquid and preheat consumption reduction system, comprise cell body, be arranged at the electric heating tube in cell body, water-cooled tube, magnetic valve, recycle pump and the heat exchanger of access cooling water source; Described cell body is provided with tank liquor outlet and tank liquor entrance; Described heat exchanger is provided with tank liquor entrance, tank liquor outlet, recirculated water entrance, circulating water outlet; Tank liquor outlet on described cell body accesses to the tank liquor entrance on heat exchanger by pipeline and via recycle pump; Tank liquor entrance on described cell body accesses to the tank liquor outlet on heat exchanger by pipeline; The water-cooled tube of described access cooling water source is via the recirculated water entrance of magnetic valve access heat exchanger; The circulating water outlet of described heat exchanger accesses to back pool by pipeline;
This system also comprises and accesses thermal water source's hot-water line and be arranged at the valve on hot-water line; Described access thermal water source's hot-water line is communicated with the water-cooled tube before magnetic valve; On described water-cooled tube, be also provided with valve.
The beneficial effects of the utility model are: in original water-cooled tube, accessing one has the hot-water line that changes into distinctive cooling backwater, by the control of valve, utilize the hot water in hot-water line through heat exchanger, tank liquor to be preheated, when being heated to after preset value, close hot-water line, switch to electrically heated; So can reduce the use of electric energy, cost-saving, and because the time of electricity consumption greatly reduces, also reduced the potential safety hazard in production process.
Brief description of the drawings
Fig. 1 is that the wire casing liquid that changes in the utility model preheats consumption reduction system architecture schematic diagram;
In figure, 1 is cell body, and 2 is electric heating tube, 3 is water-cooled tube, and 4 is magnetic valve, and 5 is recycle pump, 6 is heat exchanger, and 7 is the tank liquor outlet on cell body, and 8 is the tank liquor entrance on cell body, 9 is the tank liquor entrance on heat exchanger, and 10 is the tank liquor outlet on heat exchanger, and 11 is recirculated water entrance, 12 is circulating water outlet, 13 is hot-water line, and 14 is the valve on hot-water line, and 15 is the valve on water-cooled tube.
Embodiment
The utility model is intended to propose one and changes into wire casing liquid and preheat consumption reduction system, solves in conventional art changing into that the whole process of wire casing liquid heating is all that the electric energy consumption that adopts electrically heated mode to bring is large, cost is high and long-term electrically heated easily brings the problem of potential safety hazard.
Below in conjunction with drawings and Examples, scheme of the present utility model is further described:
As shown in Figure 1, the wire casing liquid that changes in the utility model preheats consumption reduction system, comprises cell body 1, is arranged at the electric heating tube 2 in cell body 1, water-cooled tube 3, magnetic valve 4, recycle pump 5 and the heat exchanger 6 of access cooling water source; Described cell body 1 is provided with tank liquor outlet 7 and tank liquor entrance 8; Described heat exchanger 6 is provided with tank liquor entrance 9, tank liquor outlet 10, recirculated water entrance 11, circulating water outlet 12; Tank liquor outlet 7 on described cell body 1 accesses to the tank liquor entrance 9 on heat exchanger 6 by pipeline and via recycle pump 5; Tank liquor entrance 8 on described cell body 1 accesses to the tank liquor outlet 10 on heat exchanger 6 by pipeline; The water-cooled tube 3 of described access cooling water source accesses the recirculated water entrance 11 of heat exchanger 6 via magnetic valve 4; The circulating water outlet 12 of described heat exchanger accesses to back pool by pipeline;
This system also comprises and accesses thermal water source's hot-water line 13 and be arranged at the valve 14 on hot-water line 13; Described access thermal water source's hot-water line 13 is communicated with the water-cooled tube 3 before magnetic valve 4; On described water-cooled tube 3, be also provided with valve 15.
Its principle of work is: in formed aluminum foil is produced, tank liquor temperature need to be heated to higher set temperature value (85 °), after this also need to maintain this temperature, and formation process itself is a kind of thermopositive reaction, in order to keep homo(io)thermism, also need to configure cooling recirculation system, the water-cooled tube 3 in Fig. 1 is exactly a part for described cooling recirculation system, effect is in the time that tank liquor temperature exceedes set temperature value (85 °), and tank liquor is lowered the temperature; And this temperature-fall period completes in heat exchanger 6, utilize the fluid temperature difference passing in various heat exchange pipe in heat exchanger 6 to realize heat exchange, be exactly to utilize the cold water that passes into the lesser temps in a heat transfer tube in heat exchanger 6 to lower the temperature to the tank liquor that passes into the comparatively high temps in another root heat transfer tube in heat exchanger 6 specifically, make tank liquor can maintain steady temperature value and the satisfied condition needs that change into; And the work that the tank liquor in cell body 1 is passed into heat exchanger 6 is completed by recycle pump 5; Magnetic valve 4 is for opening as required or turn-off the water coolant that passes into heat exchanger 6;
Because heat exchanger 6 is effects of playing a heat exchange, the tank liquor can utilize water coolant that temperature is lower to comparatively high temps time is lowered the temperature, and the tank liquor can certainly utilize hot water that temperature is higher to lesser temps time carries out heat temperature raising; Thereby the utility model accesses one in existing water-cooled tube 3 hot-water line 13 that changes into distinctive cooling backwater, by the control of valve, utilize the hot water in hot-water line 13 through heat exchanger 6, tank liquor to be preheated.
Its workflow is: changing into before production, when tank liquor temperature is lower, first close the valve 15 on water-cooled tube 3, the valve 14 on opens solenoid valve 4 and hot-water line 13, and ON cycle pump 5; The tank liquor that recycle pump 5 extracts in cell body 1 enters a heat transfer tube of heat exchanger 6 from the tank liquor entrance 9 of heat exchanger 6, simultaneously, hot water in hot-water line 13 enters via the recirculated water entrance 11 in heat exchanger 6 in another root heat transfer tube of heat exchanger 6, carry out heat exchange with tank liquor, tank liquor obtains heat energy, temperature increase; Tank liquor after temperature increase is got back to cell body 1 from the tank liquor outlet 10 of heat exchanger 6, and tank liquor is constantly extracted in the heat transfer tube that enters heat exchanger 6, so circulation, and the hot water entering in heat exchanger 6 enters back pool from circulating water outlet 12; So realize preheating tank liquor;
After the tank liquor in cell body rises to certain temperature (40 °), close the valve 14 on hot-water line, open the electric heater 2 in cell body 1, tank liquor is carried out to electrically heated until reach the set temperature value (85 °) that changes into reaction requirement, after this just can apply voltage to aluminium foil and change into reaction, and owing to needing heat release in formation process, in order to maintain this set temperature value (85 °), the valve 15 that needs again to open on water-cooled tube 3 is lowered the temperature to tank liquor.
Taking our company as example, before employing such scheme, changing into the each groove of line is all to carry out liquid in each groove to heat with the larger electric heating tube of power.Whole piece changes into the installation heating power of line at 600KW.As many lines use simultaneously, directly affect total load, limit to many lines and heated simultaneously, produce and incur loss through delay.And whole being heated to need consume 5000 degree nearly to fixed temperature, and in especially winter, when temperature is lower, heating electrical power consumed is larger.
Now, can adopt such scheme, while utilizing the distinctive thermal water source of my company (thermal water source's temperature is in 60 degree left and right) by former normal production, as the heat exchanger of cooling, electrolyzer be preheated.Deng reaching certain temperature (40 degree left and right), close thermal water source's valve, switch to Electric heating and heat.Can reduce like this power consumption in early stage, can multi-threadly heat simultaneously simultaneously, produce setup time shortening, particularly electric consumption reduces nearly half, greatly reduces costs, and has reduced the potential safety hazard in production process.
Claims (1)
1. change into wire casing liquid and preheat consumption reduction system, comprise cell body (1), be arranged at the electric heating tube (2) in cell body (1), water-cooled tube (3), magnetic valve (4), recycle pump (5) and the heat exchanger (6) of access cooling water source; Described cell body (1) is provided with tank liquor outlet (7) and tank liquor entrance (8); Described heat exchanger (6) is provided with tank liquor entrance (9), tank liquor outlet (10), recirculated water entrance (11), circulating water outlet (12); Tank liquor outlet (7) on described cell body (1) accesses to the tank liquor entrance (9) on heat exchanger (6) by pipeline and via recycle pump (5); Tank liquor entrance (8) on described cell body (1) accesses to the tank liquor outlet (10) on heat exchanger (6) by pipeline; The water-cooled tube (3) of described access cooling water source is via the recirculated water entrance (11) of magnetic valve (4) access heat exchanger (6); The circulating water outlet (12) of described heat exchanger accesses to back pool by pipeline;
It is characterized in that, this system also comprises and accesses thermal water source's hot-water line (13) and be arranged at the valve (14) on hot-water line (13); Described access thermal water source's hot-water line (13) water-cooled tube (3) front with magnetic valve (4) is communicated with; On described water-cooled tube (3), be also provided with valve (15).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420384320.7U CN203999870U (en) | 2014-07-11 | 2014-07-11 | Change into wire casing liquid and preheat consumption reduction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420384320.7U CN203999870U (en) | 2014-07-11 | 2014-07-11 | Change into wire casing liquid and preheat consumption reduction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203999870U true CN203999870U (en) | 2014-12-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420384320.7U Withdrawn - After Issue CN203999870U (en) | 2014-07-11 | 2014-07-11 | Change into wire casing liquid and preheat consumption reduction system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203999870U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104109890A (en) * | 2014-07-11 | 2014-10-22 | 四川石棉华瑞电子有限公司 | Formation line tank liquor preheating and consumption-reduction system and formation line tank liquor preheating and consumption-reduction method |
-
2014
- 2014-07-11 CN CN201420384320.7U patent/CN203999870U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104109890A (en) * | 2014-07-11 | 2014-10-22 | 四川石棉华瑞电子有限公司 | Formation line tank liquor preheating and consumption-reduction system and formation line tank liquor preheating and consumption-reduction method |
| CN104109890B (en) * | 2014-07-11 | 2017-04-12 | 四川石棉华瑞电子有限公司 | Formation line tank liquor preheating and consumption-reduction system and formation line tank liquor preheating and consumption-reduction method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Wang Weiguo Inventor after: Cha Hongfeng Inventor after: Gu Donghui Inventor before: Yan Qixu Inventor before: Chen Huachang Inventor before: Gu Donghui |
|
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20141210 Effective date of abandoning: 20170412 |