CN204045291U - A kind of baker for enamelled wire processing - Google Patents
A kind of baker for enamelled wire processing Download PDFInfo
- Publication number
- CN204045291U CN204045291U CN201420496837.5U CN201420496837U CN204045291U CN 204045291 U CN204045291 U CN 204045291U CN 201420496837 U CN201420496837 U CN 201420496837U CN 204045291 U CN204045291 U CN 204045291U
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- China
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- baker
- air
- enamelled wire
- wire processing
- catalytic combustion
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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Abstract
The utility model discloses a kind of baker for enamelled wire processing, comprise drying baker, electrothermal tube, catalytic combustion system, cold wind thermoregulating system, major circulatory system, hot blast switching system, waste discharge system and steam generator.The utility model is used for the baker of enamelled wire processing, and the waste gas produced in baker gathers through collecting, heat, catalytic combustion generation high temperature heat air-flow, carries out heat energy recycling; Air-heater supplements fresh air, is supplied to the oxygen of catalytic combustion abundance, drastically increases burn rate catalyst, reaches splendid environment protecting; Baker toxic emission outlet configuration waste discharge heat recovery steam generator, utilizes the waste heat of combustion gas to manufacture steam supply annealing furnace and uses, effectively saved the energy.
Description
Technical field
The utility model relates to enamelled wire technical field of processing equipment, especially relates to a kind of baker for enamelled wire processing.
Background technology
Enamelled wire is a kind of electrical material, and it is that play the effect with external insulation, enamelled wire can be processed into the lousiness line also thinner than hair by specification, cotton covered wire thick as thumb at the high-strength polyester insulating barrier of a circular copper line surface processing thin layer.In use the insulating barrier on its surface to be wiped off.Enamelled wire is applied very extensively as motor according to having good insulation effect and waterproof ability in electrical equipment, generator, water pump, electromagnet, electric welding machine, household electrical appliance, wireless telecommunications, loud speaker, telegraph, transformer etc.Enamelled wire is coated with one or more coatings on the surface of conductor, forms a kind of electric wire of tape insulation layer after curing, cooling.Enamelled wire processing can produce a large amount of waste gas in the process of curing, and any discharge of waste gas can cause the phenomenon of waste energy, contaminated environment.
Utility model content
The utility model provides a kind of baker for enamelled wire processing of a kind of energy-conserving and environment-protective.
The required technical problem solved of the utility model can be achieved through the following technical solutions:
A kind of baker for enamelled wire processing, comprise drying baker, electrothermal tube, catalytic combustion system, cold wind thermoregulating system, major circulatory system, hot blast switching system, waste discharge system and steam generator, described drying baker is arranged on the bottom of baker, is uniformly distributed electrothermal tube in described drying baker; The waste gas produced in baker in production gathers through collecting, enter catalytic combustion system after heating before catalysis carries out catalytic combustion; Generate high temperature heat air-flow after catalytic combustion, through cold wind thermoregulating system, most of heat energy is again sent in baker through major circulatory system and is carried out heat energy recycling; Another fraction heat energy burns through quadric catalysis, enters hot blast switching system after purification, and the fresh air sent in baker with air-heater carries out sufficient thermal energy exchange, and heat energy air-flow sends into drying baker; Waste gas manufactures after steam through steam generator and discharges outside baker.
Described catalytic combustion system adopts honeycomb ceramic catalytic device.
Described cold wind thermoregulating system adopts air blast to blast fresh air.
The major cycle blower fan of described major circulatory system is by Frequency Converter Control, and described major cycle fan speed is 600-1350r/m.
The air-heater of described hot blast switching system is by Frequency Converter Control, and described air-heater speed is 600-1000r/m.
Described steam generator is placed in toxic emission outlet, and steam generator manufactures steam and sends into annealing furnace.
Described baker circulating air outlet arranges air quantity adjustment air door.
It is turned down by air door that described air door is pulled outwardly, and pushing inward is opened greatly by air door.
The utility model beneficial effect is: a kind of baker for enamelled wire processing, and the waste gas produced in baker gathers through collecting, heat, catalytic combustion generation high temperature heat air-flow, carries out heat energy recycling; Air-heater supplements fresh air, is supplied to the oxygen of catalytic combustion abundance, drastically increases burn rate catalyst, reaches splendid environment protecting; Baker toxic emission outlet configuration waste discharge heat recovery steam generator, utilizes the waste heat of combustion gas to manufacture steam supply annealing furnace and uses, effectively saved the energy.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the utility model is described further:
Fig. 1 is the utility model baker structure chart.
Embodiment
In order to make practical technological means of the present utility model, creation characteristic, reach object and effect is easy to understand, below in conjunction with concrete diagram, set forth the utility model further.A kind of baker for enamelled wire processing, comprise drying baker, electrothermal tube, catalytic combustion system, cold wind thermoregulating system, major circulatory system, hot blast switching system, waste discharge system and steam generator, described drying baker is arranged on the bottom of baker, is uniformly distributed electrothermal tube in described drying baker; The waste gas produced in baker in production gathers through collecting, enter catalytic combustion system after heating before catalysis carries out catalytic combustion; Generate high temperature heat air-flow after catalytic combustion, through cold wind thermoregulating system, most of heat energy is again sent in baker through major circulatory system and is carried out heat energy recycling; Another fraction heat energy burns through quadric catalysis, enters hot blast switching system after purification, and the fresh air sent in baker with air-heater carries out sufficient thermal energy exchange, and heat energy air-flow sends into drying baker; Waste gas manufactures after steam through steam generator and discharges outside baker.
During concrete enforcement, for a baker for enamelled wire processing, comprise drying baker 1, electrothermal tube 2, heat exchange zone 3, catalysis heating 4, catalyst container 5, hot blast supplement 6, cold wind supplements 7, major cycle blower fan 8, quadric catalysis 9, steam chest 10, hot blast supplement 11, dry blower fan 12, heat-exchange tube 13, waste outlet 14, air door 15.
Drying baker 1 is arranged on the bottom of baker, is uniformly distributed electrothermal tube 2 in drying baker 1; Hot blast exchange is carried out in heat exchange zone 3; The waste gas produced in baker in production gathers through collecting, and catalysis heating 4, enters a catalyst container 5 and carry out catalytic combustion, and catalytic combustion system adopts honeycomb ceramic catalytic device, and catalyst converter is provided with splendid environmental protection and energy-saving effect from top to bottom.Generate high temperature heat air-flow after catalytic combustion, supplement 6 through hot blast and supplement hot gas, then supplement 7 through the cold wind of cold wind thermoregulating system.Cold wind thermoregulating system adopts air blast to blast fresh air, and air quantity according to ambient temperature and outlet temperature adjustment, thus plays the hot air temperature effectively regulating and send into drying baker, is that oven drying temperature is stablized.Major part heat energy is again sent in baker through the major cycle blower fan 8 of major circulatory system and is carried out heat energy recycling.The major cycle blower fan of major circulatory system is by Frequency Converter Control, and size is adjustable arbitrarily, can guarantee the constant supply of air quantity, thus ensures that oven drying temperature is balanced, and fan speed is set between 600-1350r/m.Another fraction heat energy burns through quadric catalysis 9 and produces high temperature heat air-flow.High temperature heat air-flow enters hot blast switching system after steam chest 10 purifies.The air-heater of hot blast switching system is by Frequency Converter Control, stepless speed regulation, its function uses the thermal air shutoff import cold air after exchanging, and reaches effective energy-saving effect, air-heater Speed Setting, between 600-1000r/m, regulates air-heater can change toaster entrance temperature.In hot blast switching system, high temperature heat air-flow after purification and hot blast supplement the fresh air of 11 feedings and dry blower fan 12 and blast gas sufficient thermal energy exchange after heat-exchange tube 13 exchanges, and the heat energy supplemented is fresh air, more be supplied to the oxygen of catalytic combustion abundance, drastically increase burn rate catalyst, reach splendid environment protecting.Heat energy air-flow after exchange sends into drying baker 1.The waste gas produced manufactures through steam generator again discharges outside baker after steam, and steam generator is placed in toxic emission outlet 14, and steam generator manufactures steam and sends into annealing furnace.The outlet of baker circulating air is provided with every bar line independently air quantity adjustment air door 15, this air door adjustable sends into hot blast rate in baker, thus reaching the object that adjustment oven drying temperature is balanced and line look unified, it is turned down by air door that air door is pulled outwardly, and pushing inward is opened greatly by air door.
More than show and describe general principle of the present utility model, principal character and advantage of the present utility model.The technical staff of the industry should understand; the utility model is not restricted to the described embodiments; what describe in above-described embodiment and specification just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope, the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (9)
1. the baker for enamelled wire processing, it is characterized in that: comprise drying baker, electrothermal tube, catalytic combustion system, cold wind thermoregulating system, major circulatory system, hot blast switching system, waste discharge system and steam generator, described drying baker is arranged on the bottom of baker, is uniformly distributed electrothermal tube in described drying baker; The waste gas that baker produces gathers through collecting, enter catalytic combustion system after heating before catalysis carries out catalytic combustion; Generate high temperature heat air-flow after catalytic combustion, through cold wind thermoregulating system, most of heat energy is again sent in baker through major circulatory system and is carried out heat energy recycling; Another fraction heat energy burns through quadric catalysis, enters hot blast switching system after purification, and the fresh air sent in baker with air-heater carries out sufficient thermal energy exchange, and heat energy air-flow sends into drying baker; Waste gas manufactures after steam through steam generator and discharges outside baker.
2., according to a kind of baker for enamelled wire processing according to claim 1, it is characterized in that: described catalytic combustion system adopts honeycomb ceramic catalytic device.
3., according to a kind of baker for enamelled wire processing according to claim 2, it is characterized in that: described catalyst converter is installed from top to down.
4. according to a kind of baker for enamelled wire processing according to claim 1, it is characterized in that: described cold wind thermoregulating system adopts air blast to blast fresh air.
5., according to a kind of baker for enamelled wire processing according to claim 1, it is characterized in that: the major cycle blower fan of described major circulatory system is by Frequency Converter Control, and described major cycle fan speed is 600-1350r/m.
6., according to a kind of baker for enamelled wire processing according to claim 1, it is characterized in that: the air-heater of described hot blast switching system is by Frequency Converter Control, and described air-heater speed is 600-1000r/m.
7. according to a kind of baker for enamelled wire processing according to claim 1, it is characterized in that: described steam generator is placed in toxic emission outlet, and steam generator manufactures steam and sends into annealing furnace.
8. according to a kind of baker for enamelled wire processing according to claim 1, it is characterized in that: described baker circulating air outlet arranges air quantity adjustment air door.
9., according to a kind of baker for enamelled wire processing according to claim 8, it is characterized in that: it is turned down by air door that described air door is pulled outwardly, pushing inward is opened greatly by air door.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420496837.5U CN204045291U (en) | 2014-08-29 | 2014-08-29 | A kind of baker for enamelled wire processing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420496837.5U CN204045291U (en) | 2014-08-29 | 2014-08-29 | A kind of baker for enamelled wire processing |
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| Publication Number | Publication Date |
|---|---|
| CN204045291U true CN204045291U (en) | 2014-12-24 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420496837.5U Expired - Fee Related CN204045291U (en) | 2014-08-29 | 2014-08-29 | A kind of baker for enamelled wire processing |
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| CN (1) | CN204045291U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105374473A (en) * | 2014-08-29 | 2016-03-02 | 安徽九华金润铜业有限公司 | Baking oven for processing of enameled wire |
-
2014
- 2014-08-29 CN CN201420496837.5U patent/CN204045291U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105374473A (en) * | 2014-08-29 | 2016-03-02 | 安徽九华金润铜业有限公司 | Baking oven for processing of enameled wire |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141224 Termination date: 20170829 |