CN201748765U - Drying device utilizing residual heat - Google Patents
Drying device utilizing residual heat Download PDFInfo
- Publication number
- CN201748765U CN201748765U CN201020272190XU CN201020272190U CN201748765U CN 201748765 U CN201748765 U CN 201748765U CN 201020272190X U CN201020272190X U CN 201020272190XU CN 201020272190 U CN201020272190 U CN 201020272190U CN 201748765 U CN201748765 U CN 201748765U
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- Prior art keywords
- waste gas
- heat
- chamber
- pipe
- heat exchanger
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Abstract
The utility model relates to a drying device utilizing residual heat, which comprises a waste gas inlet pipe, a waste gas outlet pipe and a drying chamber, wherein a heat exchanger is arranged between the waste gas inlet pipe and the waste gas outlet pipe, the heat exchanger comprises a heat exchange chamber and a heat dissipation chamber, the heat exchange chamber and the heat dissipation chamber are mutually sealed and isolated by a partition board, the partition board is provided with a group of heat exchange pipes, one end of the heat exchange pipe extends into the heat exchange chamber, and the other end of the heat exchange pipe extends to the heat dissipation chamber; and the waste gas inlet pipe and the waste gas outlet pipe are respectively connected at both sides of the heat exchange chamber, both sides of the heat dissipation chamber are respectively connected with an air inlet pipe and an air outlet pipe, the air outlet pipe is connected with a fan, and an air outlet of the fan is connected with the drying chamber. The utility model can reasonably transform heat energy of high-temperature waste gas for use, improves the production efficiency, saves production materials, reduces the production cost, protects the environment, meets the requirement of sustainable development and is suitable for popularization and the application.
Description
Technical field
The utility model relates to a kind of heated-air drying equipment, especially a kind of UTILIZATION OF VESIDUAL HEAT IN drying equipment.
Background technology
Battery separator need carry out drying processing by hyperthermia drying equipment when producing, the equipment that is used at present the battery separator oven dry on the market mainly is by coal combustion, fuel such as diesel oil provide hot blast to carry out bake drying, when providing hot blast to dry, these fuel combustions can produce a large amount of high-temp waste gas, flue gas, the equipment that at present these high-temp waste gas is utilized does not also have, use then can have a strong impact on the quality of product if high-temp waste gas directly is transmitted back in the drying chamber, if high-temp waste gas directly is discharged in the atmosphere, then pollutes the environment and increase the weight of greenhouse effects.Be badly in need of at present a kind of waste gas heat utilization drying equipment that the high-temp waste gas heat rationally can be transformed use occurring, satisfy the demand that sustainable development is produced.
Summary of the invention
The utility model will solve the shortcoming of above-mentioned prior art, and a kind of UTILIZATION OF VESIDUAL HEAT IN drying equipment that the high-temp waste gas heat rationally can be transformed use is provided, and has satisfied the demand of producing.
The utility model solves the technical scheme that its technical problem adopts: this UTILIZATION OF VESIDUAL HEAT IN drying equipment, comprise that waste gas access tube, waste gas pick out pipe, drying chamber, waste gas access tube and waste gas pick out and are provided with heat exchanger between the pipe, described heat exchanger comprises Heat Room, heat dissipation chamber, Heat Room and heat dissipation chamber are through the mutual seal isolation of dividing plate, dividing plate is provided with one group of heat exchanger tube, and heat exchanger tube one end stretches to Heat Room, and the other end stretches to heat dissipation chamber; Waste gas access tube, waste gas pick out pipe and are connected on the Heat Room both sides respectively, and the heat dissipation chamber both sides are connected to the air access tube respectively, air picks out pipe, and air picks out and is connected to blower fan on the pipe, and the air outlet of blower fan is connected with drying chamber.Like this, just the high-temp waste gas that fuel combustion produces directly can be fed the waste gas access tube, the heat exchanger tube that enters in Heat Room and the Heat Room of high-temp waste gas contacts then, heat exchanger tube with the thermal energy conduction of high-temp waste gas in heat dissipation chamber, air enters pipe by air and enters heat dissipation chamber and contact with heat exchanger tube, heat exchanger tube is with the heat transferred air, and hot-air is transported to drying chamber by blower fan and dries effect, reaches the purpose of UTILIZATION OF VESIDUAL HEAT IN drying.
Further, waste gas picks out to manage and is connected with the chimney tower.Like this, through the waste gas allow compliance with emission standards after the UTILIZATION OF VESIDUAL HEAT IN, and dust picks out in the pipe at chimney tower and waste gas through the cooling postprecipitation mostly, and is free from environmental pollution.Heat exchanger tube is provided with the spiral condensate film outward.Can strengthen intensity and uptake that heat exchanger tube absorbs heat like this, guarantee fully to recycle the heat energy of high-temp waste gas.
The effect that the utility model is useful is: of the present utility model rational in infrastructure, by heat exchanger tube with the heat of high-temp waste gas conduct in the heat dissipation chamber in conjunction with clean normal air, air themperature is raise, act on hot-air being transported in the drying chamber, thereby reach the purpose of UTILIZATION OF VESIDUAL HEAT IN drying by blower fan.The utility model can reasonably transform high-temp waste gas heat energy and use, and enhances productivity, and saves the means of production, reduces production costs, and environmental protection again simultaneously meets the sustainable development requirement, is fit to apply.
Description of drawings
Fig. 1 is a structural representation of the present utility model;
Structural representation when Fig. 2 analyses and observe after partly amplifying for A among Fig. 1.
Description of reference numerals: waste gas access tube 1, waste gas pick out pipe 2, drying chamber 3, heat exchanger 4, Heat Room 5, heat dissipation chamber 6, dividing plate 7, heat exchanger tube 8, air access tube 9, air pick out pipe 10, blower fan 11, chimney tower 12, spiral condensate film 13.
The specific embodiment
The utility model is described in further detail below in conjunction with accompanying drawing:
With reference to accompanying drawing: this UTILIZATION OF VESIDUAL HEAT IN drying equipment in the present embodiment, comprise that waste gas access tube 1, waste gas pick out pipe 2, drying chamber 3, waste gas access tube 1 and waste gas pick out between the pipe 2 and are provided with heat exchanger 4, described heat exchanger 4 comprises Heat Room 5, heat dissipation chamber 6, Heat Room 5 and heat dissipation chamber 6 are through dividing plate 7 mutual seal isolation, dividing plate 7 is provided with one group of heat exchanger tube 8, and heat exchanger tube 8 one ends stretch to Heat Room 5, and the other end stretches to heat dissipation chamber 6; Waste gas access tube 1, waste gas pick out pipe 2 and are connected on Heat Room 5 both sides respectively, and heat dissipation chamber 6 both sides are connected to air access tube 9 respectively, air picks out pipe 10, and air picks out on the pipe 10 and is connected to blower fan 11, and the air outlet of blower fan 11 is connected with drying chamber 3.Waste gas picks out pipe 2 and is connected with chimney tower 12.The heat exchanger tube 8 outer spiral condensate films 13 that are provided with.
During use, the high-temp waste gas that fuel combustion produces directly can be fed waste gas access tube 1, the heat exchanger tube 8 that enters in Heat Room 5 and the Heat Room 5 of high-temp waste gas contacts then, heat exchanger tube 8 arrives the thermal energy conduction of high-temp waste gas in the heat dissipation chamber 6, air enters pipe 9 by air and enters heat dissipation chamber 6 and contact with heat exchanger tube 8, heat exchanger tube 8 is with the heat transferred air, and hot-air is transported to oven dry Room 3 by blower fan 11 and dries effect, reaches the purpose of UTILIZATION OF VESIDUAL HEAT IN drying.
The heat exchanger tube 8 outer spiral condensate films 23 that add make whole heat exchanger 4 strengthen intensity and the uptake that absorbs heat, and the heat energy of high-temp waste gas is made full use of more.
Though the utility model illustrates and describes by the reference preferred embodiment,, those skilled in the art should understand, and in the scope of claims, can do the various variation on form and the details.
Claims (3)
1. UTILIZATION OF VESIDUAL HEAT IN drying equipment, comprise that waste gas access tube (1), waste gas pick out pipe (2), drying chamber (3), described waste gas access tube (1) and waste gas pick out and are provided with heat exchanger (4) between the pipe (2), it is characterized in that: described heat exchanger (4) comprises Heat Room (5), heat dissipation chamber (6), described Heat Room (5) and heat dissipation chamber (6) are through the mutual seal isolation of dividing plate (7), described dividing plate (7) is provided with one group of heat exchanger tube (8), described heat exchanger tube (8) one ends stretch to Heat Room (5), and the other end stretches to heat dissipation chamber (6); Described waste gas access tube (1), waste gas pick out pipe (2) and are connected on Heat Room (5) both sides respectively, described heat dissipation chamber (6) both sides are connected to air access tube (9) respectively, air picks out pipe (10), described air picks out and is connected to blower fan (11) on the pipe (10), and the air outlet of described blower fan (11) is connected with drying chamber (3).
2. UTILIZATION OF VESIDUAL HEAT IN drying equipment according to claim 1 is characterized in that: described waste gas picks out pipe (2) and is connected with chimney tower (12).
3. UTILIZATION OF VESIDUAL HEAT IN drying equipment according to claim 1 is characterized in that: the outer spiral condensate film (13) that is provided with of described heat exchanger tube (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201020272190XU CN201748765U (en) | 2010-07-27 | 2010-07-27 | Drying device utilizing residual heat |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201020272190XU CN201748765U (en) | 2010-07-27 | 2010-07-27 | Drying device utilizing residual heat |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201748765U true CN201748765U (en) | 2011-02-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201020272190XU Expired - Fee Related CN201748765U (en) | 2010-07-27 | 2010-07-27 | Drying device utilizing residual heat |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201748765U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102927809A (en) * | 2012-11-26 | 2013-02-13 | 蒋建新 | Dryer capable of using boiler afterheat |
| CN105241260A (en) * | 2015-10-30 | 2016-01-13 | 浙江长兴振明高科耐火材料有限公司 | Drying device for producing fireproofing materials |
| CN105277001A (en) * | 2015-10-30 | 2016-01-27 | 浙江长兴振明高科耐火材料有限公司 | Production method of refractory material |
| CN105277000A (en) * | 2015-10-30 | 2016-01-27 | 浙江长兴振明高科耐火材料有限公司 | Heat recycling device of calcining kiln |
| CN106474753A (en) * | 2016-03-24 | 2017-03-08 | 梅丽中 | A kind of bittern crystallizing and drying device |
-
2010
- 2010-07-27 CN CN201020272190XU patent/CN201748765U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102927809A (en) * | 2012-11-26 | 2013-02-13 | 蒋建新 | Dryer capable of using boiler afterheat |
| CN105241260A (en) * | 2015-10-30 | 2016-01-13 | 浙江长兴振明高科耐火材料有限公司 | Drying device for producing fireproofing materials |
| CN105277001A (en) * | 2015-10-30 | 2016-01-27 | 浙江长兴振明高科耐火材料有限公司 | Production method of refractory material |
| CN105277000A (en) * | 2015-10-30 | 2016-01-27 | 浙江长兴振明高科耐火材料有限公司 | Heat recycling device of calcining kiln |
| CN105277001B (en) * | 2015-10-30 | 2018-08-03 | 浙江长兴振明高科耐火材料有限公司 | A kind of production method of refractory material |
| CN106474753A (en) * | 2016-03-24 | 2017-03-08 | 梅丽中 | A kind of bittern crystallizing and drying device |
| CN106474753B (en) * | 2016-03-24 | 2019-01-29 | 青岛果子知识产权运营有限公司 | A kind of brine crystallizing and drying device |
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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: 20110216 Termination date: 20180727 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |